WO2007022732A1 - A composite slow-release coated fertilizer without environmental pollution - Google Patents
A composite slow-release coated fertilizer without environmental pollution Download PDFInfo
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- WO2007022732A1 WO2007022732A1 PCT/CN2006/002183 CN2006002183W WO2007022732A1 WO 2007022732 A1 WO2007022732 A1 WO 2007022732A1 CN 2006002183 W CN2006002183 W CN 2006002183W WO 2007022732 A1 WO2007022732 A1 WO 2007022732A1
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- WIPO (PCT)
- Prior art keywords
- film layer
- sulfur
- urea
- melamine
- friendly composite
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- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05G—MIXTURES OF FERTILISERS COVERED INDIVIDUALLY BY DIFFERENT SUBCLASSES OF CLASS C05; MIXTURES OF ONE OR MORE FERTILISERS WITH MATERIALS NOT HAVING A SPECIFIC FERTILISING ACTIVITY, e.g. PESTICIDES, SOIL-CONDITIONERS, WETTING AGENTS; FERTILISERS CHARACTERISED BY THEIR FORM
- C05G5/00—Fertilisers characterised by their form
- C05G5/30—Layered or coated, e.g. dust-preventing coatings
- C05G5/36—Layered or coated, e.g. dust-preventing coatings layered or coated with sulfur
Definitions
- the invention relates to a coated slow release fertilizer, in particular to an environmentally friendly composite coated slow release fertilizer, belonging to the field of fertilizer industry.
- slow release fertilizer is the development direction of the world fertilizer industry.
- coated slow release fertilizer is the development focus of slow release fertilizer, but the envelope of non-degradable coated slow release fertilizer will be polluted by the environment, so the environmental protection package of degradable envelope is developed.
- Membrane slow release fertilizer meets the requirements of environmental protection and social sustainable development, and will become the mainstream of slow release fertilizer in the future.
- the degradable material has a high permeable and transdermal speed, so the release period of the prepared degradable coated slow-release fertilizer is very short, generally only a few days, such as the sustained release of the envelope type using a urea-formaldehyde resin coating.
- a coated slow release fertilizer coated with fertilizer and lignin modified material is a difficult problem to be solved for the degradable coated slow release fertilizer, and it is also the key to the practical application of the degradable coated slow release fertilizer in the future.
- the technical solution for achieving the object of the present invention is: an environmentally friendly composite coated slow release fertilizer consisting of a fertilizer core and a coating on the outer side of the fertilizer core, the envelope comprising: (a) a sulfur film layer, (b) a sulfur-containing film Degrading the polymer mixture film layer and/or the degradable polymer film layer, with or without (c) a high barrier organic film layer; wherein the sulfur film layer is the inner or intermediate layer of the entire envelope.
- the average mass fraction of sulfur may be 0% to 95%, preferably 20% to 90%.
- the degradable polymer used in the environmentally friendly composite coated slow release fertilizer of the invention is a water-insoluble degradable polymer, and may be an amino resin, an acetal resin of polyvinyl alcohol and a copolymer thereof, an unsaturated oleoresin and One or more of natural polymers and derivatives thereof.
- the natural polymer and the derivative thereof may be one or more of nitrocellulose, shellac, cellulose acetate, crosslinked starch, chitin derivative, lignin derivative, and the like.
- the high barrier organic film layer in the environmentally friendly composite coated slow release fertilizer coating of the present invention is preferably a non-polar organic film layer.
- the material of the non-polar organic film layer may be a non-polar low molecular weight organic substance and/or a non-polar polymer, wherein the non-polar organic film layer is preferably a non-polar low molecular weight organic substance.
- the non-polar organic film layer is preferably adhered to the sulfur film layer, and the non-polar organic film layer is preferably not the outermost film layer of the envelope.
- the non-polar low molecular weight organic substance may be one or more of a wax having a melting point of 40 ° C, a melting point or a softening point of 40 ° C and a polyolefin or polystyrene having a molecular weight of ⁇ 2000 and a petroleum resin having a softening point of 40 ⁇ .
- the non-polar polymer may be a polyolefin or a polyphenylene Ethylene, butadiene rubber, natural rubber, polyisoprene rubber, styrene butadiene rubber, butyl rubber, ethylene propylene rubber and ethylene propylene diene rubber, styrene butadiene styrene block copolymer and styrene One or more of an isoprene-styrene block copolymer and the like.
- the high barrier organic film layer of the environmentally friendly composite coated slow release fertilizer of the present invention may contain a sustained release modifier.
- the sustained release modifier is preferably a polar organic substance which is soluble in the material of the high barrier organic film layer.
- the environmentally friendly composite coated slow-release fertilizer of the invention has a total average thickness of 10 ⁇ 180 ⁇ m, wherein the average thickness of the sulfur film layer can be from 1 to 100 m, the degradable polymer film layer and the sulfur-containing degradable polymerization layer.
- the total average thickness of the film mixture layer may be 5 to 180 / m, the total average thickness of the high barrier organic film layer may be 0 to 15 m, and the average thickness of the outer layer of the sulfur film layer is not less than 3 m;
- the total average thickness of the sulfur-containing degradable polymer mixture film layer is 0 to 100 m, and the total average thickness of the degradable polymer film layer is 0 to 100 m.
- the total average thickness of the coating is preferably from 20 to 90 m, wherein the average thickness of the sulfur film layer is preferably from 8 to 60/m, and both the degradable polymer film layer and the sulfur-containing degradable polymer mixture film layer are The total average thickness is preferably 8 ⁇ 50/m, the total average thickness of the high barrier organic film layer is preferably 0 ⁇ 10/m, and the average thickness of the outer layer of the sulfur film layer is preferably not less than 5/m;
- the total average thickness of the film layer of the sulfur degradable polymer mixture is preferably from 8 to 50 ⁇ , and the total average thickness of the degradable polymer film layer is preferably from 0 to 35 ⁇ m.
- the environmental protection composite coated slow release fertilizer of the invention uses degradable polymer and sulfur as all or main coating materials, and all the coating materials have no pollution to the environment or little pollution, so it is a completely or almost completely environmentally friendly slow release fertilizer.
- the coating has no composite non-polar polymer film layer, it is a completely environmentally friendly slow-release fertilizer.
- the environmentally friendly composite coated slow release fertilizer of the invention is combined with a sulfur film layer by using a degradable polymer film layer and/or a sulfur-containing degradable polymer mixture film layer, because the sulfur film layer has high barrier to water and fertilizer, and at the same time Since the degradable polymer is water-insoluble, it does not dissolve in the soil when the fertilizer is applied to the soil, and the degradable polymer film layer and/or the sulfur-containing degradable polymer mixture film layer can always be used throughout the use process.
- the membrane barrier effect, and thus the degradable coated slow release fertilizer of the present invention using a degradable polymer as a coating material can have a long release period.
- urea-formaldehyde resins and melamine-formaldehyde resins are relatively inexpensive degradable polymers, which are much cheaper than conventional refractory polymers, and which are themselves slow-release nitrogen fertilizers, urea-formaldehyde resins and melamine-formaldehyde resins.
- the nitrogen content is about 30% and 54% respectively, and the nitrogen content of the melamine-formaldehyde resin is higher than the nitrogen content of urea (about 45%).
- the invention relates to an environmentally-friendly composite coated slow-release fertilizer which is completely fertilizer-fermented slow-release fertilizer with high fertilizer content and low cost.
- the cost index of pure fertilizer is about 50
- the cost index of urea-formaldehyde resin and melamine-formaldehyde resin is about 450 and 600, respectively, 85% of fertilizer, 10% of sulfur and urethane resin.
- the 5% melamine-formaldehyde resin composition of the environmentally friendly composite coated slow release fertilizer of the present invention is calculated as an example, and their total cost index is about 112.5 and 120, only 12.5% ⁇ 20% higher than the cost of pure fertilizer, can be used as a common agricultural field fertilizer.
- the barrier property of the sulfur-containing degradable polymer mixture film to water and fertilizer is simpler than The degradable polymer film layer is strong, especially when the sulfur content is ⁇ (such as 80% ⁇ 90%), the barrier property to water and fertilizer is strong, so there is a film layer of sulfur-containing degradable polymer mixture in the coating film.
- the environmentally friendly composite coated slow release fertilizer of the invention has a longer release period, especially when the sulfur-containing degradable polymer mixture film layer is in close contact with the sulfur film layer.
- the use of the sulfur-containing degradable polymer mixture film layer can further reduce the amount of the degradable polymer, and the cost is lower.
- the invention can be made in the coating of the environmentally friendly composite coated slow release fertilizer of the present invention by recombining a very thin high barrier organic film layer (the amount of which is small, which is smaller than the amount of the sulfur film layer which can be separately protected).
- the release period of the environmentally friendly composite coated slow release fertilizer is further prolonged, especially when the high barrier organic film layer is a non-polar organic film layer, and the non-polar organic film layer is closely attached to the sulfur film layer, the effect is obvious. Therefore, the release period of the environmentally friendly composite coated slow release fertilizer of the present invention in which the non-polar organic film layer is compounded in the envelope can be long.
- a polar organic substance or other slow release modifier which is soluble in the high barrier organic film layer material is added to the high barrier organic film layer, and the release period can be freely adjusted by controlling the addition amount, and the coating film is changed more than the coating film.
- the method of adjusting the release period of the total thickness of the layer is more efficient and more economical.
- a non-polar low molecular weight organic material such as wax, polyolefin or polystyrene having a molecular weight of ⁇ 2000, and petroleum resin, non-polar low molecular weight organic substances are generally available in the environment.
- the environmentally friendly composite coated slow release fertilizer of the present invention is still a completely environmentally friendly slow release fertilizer. Even if the non-polar organic film layer material uses a non-polar polymer, since it is used in an amount of only about 1%, it has little environmental pollution compared with the slow-release fertilizer of the prior art, and has obvious advantages. .
- FIG. 1 is a structural view of a spherical fertilizer core 1 - a sulfur-containing degradable polymer mixture film - a sulfur film layer 2 - a sulfur-containing degradable polymer mixture film layer 3 of the environmentally friendly composite film type slow release fertilizer of the present invention.
- Fig. 2 is a structural view of a spherical fertilizer core 1 - sulfur film layer 2 - sulfur-containing degradable polymer mixture film layer 3 of the environmentally friendly composite film type slow release fertilizer of the present invention.
- Fig. 3 is a structural view of a spherical fertilizer core 1 - a degradable polymer film layer 4 - a sulfur film layer 2 - a degradable polymer film layer 4 of the environmentally friendly composite film type slow release fertilizer of the present invention.
- Fig. 4 is a structural view of a spherical fertilizer core 1 - sulfur film layer 2 - a degradable polymer film layer 4 of the environmentally friendly composite coated slow release fertilizer of the present invention.
- Fig. 5 is a structural view of a spherical fertilizer core 1 - sulfur-degradable polymer mixture film 3 - sulfur film layer 2 - degradable polymer film layer 4 of the environmentally friendly composite film type slow release fertilizer of the present invention.
- Figure 6 is a spherical fertilizer core 1 of the environmentally friendly composite coated slow release fertilizer of the present invention, a degradable polymer film layer 4 sulfur Sulfide layer 2 - structure diagram of film layer 3 of sulfur-containing degradable polymer mixture.
- spherical fertilizer core 1 of a sulfur-containing degradable polymer mixture layer of the environmentally friendly composite coated slow release fertilizer of the present invention 3 - a sulfur film layer 2 - a sulfur-containing degradable polymer mixture film layer 3 - a degradable polymer Structure of the film layer 4.
- Fig. 8 is a structural view of a spherical fertilizer core 1 - sulfur film layer 2 - sulfur-degradable polymer mixture film layer 3 - degradable polymer film layer 4 of the environmentally friendly composite film type slow release fertilizer of the present invention.
- Figure 10 is a spherical fertilizer core 1 of a sulfur-containing degradable polymer mixture of the environmentally friendly composite coated slow release fertilizer of the present invention.
- 3 Sulfur film layer 2 - High barrier organic film layer 5 - Degradable polymer film layer 4 Structure diagram.
- Figure 11 is a structural view of a spherical fertilizer core 1 - a high barrier organic film layer 5 - a sulfur film layer 2 - a sulfur-containing degradable polymer mixture film layer 3 of the environmentally friendly composite film type slow release fertilizer of the present invention.
- Fig. 12 is a structural view of a spherical fertilizer core 1 - a high barrier organic film layer 5 - a sulfur film layer 2 - a degradable polymer film layer 4 of the environmentally friendly composite film type slow release fertilizer of the present invention.
- the environmentally friendly composite coated slow release fertilizer of the present invention is composed of a fertilizer core 1 and a coating film outside the fertilizer core, and the coating film comprises (a) a sulfur film layer 2, (b) a sulfur-containing degradable polymer mixture film layer 3 and I or Degradable polymer film layer 4, with or without (c) high barrier organic film layer 5; wherein the sulfur film layer is the inner or intermediate layer of the entire envelope.
- the fertilizer core of the environmentally friendly composite coated slow release fertilizer of the invention may be nitrogen fertilizer, phosphate fertilizer, potassium fertilizer or compound fertilizer.
- the shape of the fertilizer core may be granular, flake, or the like, but it is preferably granular, and preferably spherical.
- the film of the sulfur-containing degradable polymer mixture in the present invention means a film layer of a mixture of sulfur and a degradable polymer.
- the coating of the environmentally friendly composite coated slow release fertilizer of the present invention may be a composite film layer of a sulfur-containing degradable polymer mixture film layer and a sulfur film layer, and such a composite film layer is preferred.
- the structure of the slow release fertilizer can be as shown in Fig. 1 and Fig. 2, and the structure of Fig. 1 is superior to that of Fig. 2.
- the envelope of the environmentally friendly composite coated slow release fertilizer of the present invention may also be a composite film layer of a degradable polymer film layer and a sulfur film layer.
- the structure of the slow-release fertilizer can be as shown in Fig. 3 and Fig. 4, and the structure of Fig. 3 is superior to that of Fig. 4.
- the coating of the environmentally friendly composite coated slow release fertilizer of the present invention may also be a composite film layer of a sulfur-containing degradable polymer mixture film layer, a degradable polymer film layer and a sulfur film layer.
- the structure of the sulfur-containing degradable polymer mixture film layer is close to the sulfur film layer, and the film layer of the sulfur-containing degradable polymer mixture is close to the surface of the sulfur film layer than the sulfur-containing degradable polymer mixture film layer.
- the structure close to the outer surface of the sulfur film layer is excellent.
- the structure of the slow release fertilizer can be as shown in Fig. 5, Fig. 6, Fig. 7, and Fig. 8. Among them, Fig. 5 and Fig.
- the coating of the environmentally friendly composite coated slow release fertilizer of the present invention can further compound a high barrier organic film layer in each of the above three types of structures.
- the high barrier organic film layer refers to a film layer having a lower transmittance to water and fertilizer than the degradable polymer film layer, that is, the high barrier organic film layer material has a lower transmittance to water and fertilizer than in the envelope film.
- the non-polar organic film layer has a low transmittance to water and fertilizer, water and fertilizer are mainly transmitted through the film defect, so the high-barrier organic film layer in the environmentally friendly composite coated slow release fertilizer coating of the present invention It is preferably a non-polar organic film layer. Further, the non-polar organic film layer is preferably adhered to the sulfur film layer, and the non-polar organic film layer is preferably not the outermost film layer of the envelope.
- the structure of the sulfur-containing degradable polymer mixture film layer adhering to the sulfur film layer is a preferred structure.
- the non-polar organic film layer is closely attached to the sulfur film layer, and the sulfur-containing degradable polymer mixture film layer is more closely adhered to the sulfur film layer, and the non-polar organic film layer is more preferred.
- the structure closely adjacent to the sulfur film layer is a more preferable structure.
- the inner surface and the outer surface of the sulfur film layer may be combined with a non-polar organic film layer.
- the non-polar low molecular weight organic film layer is generally on the outer surface of the sulfur film layer; the non-polar polymer is on the inner surface and the outer surface of the sulfur film layer, However, it is generally only available on one side, and the barrier effect exerted on the inner surface is better.
- the film layer of the sulfur-containing degradable polymer mixture is closely attached to the non-attached non-paste layer.
- the other surface of the sulfur film layer of the polar organic film layer and/or the structure which is in close contact with the surface of the non-polar organic film layer is a more optimized structure among them.
- the structure shown in Fig. 9 to Fig. 12 is four representative structures of the environmentally friendly composite coated type slow release fertilizer of the present invention which is compounded with a high barrier organic film layer. It can also be a structure of other combinations.
- Figs. 1 to 12 it is also possible to change the structure based on the structures of Figs. 1 to 12.
- it may be a multiple composite structure of the envelope structure shown in Figs. 1 to 12, or a multiple composite structure in which the envelope structures shown in Figs. 1 to 12 are combined with each other.
- these multiple composite structures are not preferred structures from a process perspective.
- the average mass fraction of sulfur may be between 0% and 95%.
- the sulfur content is too low, the effect of improving the barrier property of the film layer is not obvious, but when the content is too high, the toughness of the film layer is low and brittle, so it is preferably between 20% and 90%, preferably 60%. Between ⁇ 90%. If necessary, a certain amount of plasticizer may be added to the film layer of the sulfur-containing degradable polymer mixture to increase the toughness of the film.
- the sulfur-containing degradable polymer mixture film layer of the sulfur-containing degradable polymer mixture for example, the sulfur content in the film layer of the sulfur-containing degradable polymer mixture outside the sulfur film layer (ie, opposite to the direction toward the fertilizer core).
- the outer layer has a low sulfur content to give the outer layer high toughness.
- the sulfur-containing degradable polymer mixture film layer outside the sulfur film layer is high, for example, 80% or more, the sulfur-containing degradable polymer mixture film layer may have a thin layer (such as 3 ⁇ 10 ⁇ ⁇ ). A layer of degradable polymer film to better protect the inner film layer.
- the biodegradable composite film type slow release fertilizer of the invention adopts a degradable polymer, which can be an amino resin or a polyethylene.
- a degradable polymer which can be an amino resin or a polyethylene.
- the natural polymer and its derivative may be one or more of nitrocellulose, shellac, cellulose acetate, crosslinked starch, chitin derivative, and lignin derivative.
- the degradable polymer in the environmentally friendly composite coated slow release fertilizer coating of the present invention is water-insoluble, or although the prepolymer used is water-soluble, the degradable polymer in the finally formed film layer should be non-water soluble.
- the prepolymer such as a urea-formaldehyde resin and a melamine-formaldehyde resin may be water-soluble, but the urea-formaldehyde resin and the melamine-formaldehyde resin formed by curing cross-linking become water-insoluble.
- amino resins are preferred, especially urea-formaldehyde resins and melamine-formaldehyde resins (including modified urea-formaldehyde resins and modified melamine-formaldehyde resins) at low prices, and they are used as degradable polymerization.
- the environmentally-friendly composite coated slow-release fertilizer prepared by the material of the coating material is a complete fertilizer-fermented slow-release fertilizer with high fertilizer content and low product cost; in particular, the resistance of melamine-formaldehyde resin to water and fertilizer
- the permeability is relatively strong, and its degradation rate is slow, and its envelope can exert an envelope barrier effect for a long period of time.
- the unsaturated oleoresin is a resin obtained by crosslinking an unsaturated oil, and a solvent may not be used in the process of coating the unsaturated oil, so that an unsaturated oleoresin may also be preferred.
- Unsaturated oil refers to a natural oil that contains a double bond in the molecular structure and can undergo a cross-linking reaction, such as tung oil, soybean oil, linseed oil or dehydrated castor oil. Among them, tung oil is a lower-priced natural unsaturated oil.
- the tung oil resin film formed in combination has a strong barrier property against water and fertilizer, and is a preferred unsaturated oil.
- acetal acetal resin 50% acetal degree
- nitrocellulose of the water-insoluble polyvinyl alcohol and its copolymer are also degradable coating materials which are considered to be selected.
- the acetal resin of polyvinyl alcohol and its copolymer may be a formal resin, a acetal resin or a butyral resin of polyvinyl alcohol and a copolymer thereof.
- a low molecular organic substance such as a sulfur-containing degradable polymer mixture film layer and a degradable polymer film layer may be added.
- a small amount of a bactericide or a bacteriostatic agent may be added to the aforementioned plasticizer or the like.
- the high-barrier organic film layer material may be a ruthenium-blocking low-molecular organic substance or It is a highly barrier-resistant, refractory polymer.
- the high-barrier low-molecular organic substance may be a low-permeability organic substance (relative to a degradable polymer) such as pitch and a mixture thereof and rosin (ester) and a mixture thereof, and the high-barrier refractory polymer may be propylene.
- Low permeability polymer (relative to degradable polymers) such as nitrile-butadiene-styrene copolymer (ABS), nitrile rubber, unsaturated polyester, polyurethane and epoxy resin.
- the high-barrier organic film layer is preferably a non-polar organic film layer, and the non-polar organic film layer is preferably in close contact with the sulfur film layer, and is preferably not the outermost film layer of the envelope.
- the material of the non-polar organic film layer may be a non-polar low molecular weight organic substance and an I or a non-polar polymer, wherein the non-polar organic film layer is preferably a non-polar low molecular weight organic substance.
- the nonpolar polar molecular layer used in the nonpolar organic film layer has
- the organic substance may be one or more of a wax having a melting point of ⁇ 40, a melting point or a low molecular weight polyolefin or polystyrene having a melting point of ⁇ 40 ° C and a molecular weight of ⁇ 2000, and a petroleum resin having a softening point of ⁇ 40 ⁇ .
- the wax may be a petroleum wax, a synthetic wax, a natural wax, a mineral wax or the like;
- the low molecular weight polyolefin may be a polyethylene wax, or may be a low molecular weight polypropylene, a low molecular weight polyisobutylene or the like.
- the molecular weight of the low molecular weight polyolefin or polystyrene may also be ⁇ 2000.
- the melting point or softening point of the non-polar low molecular weight organic substance is preferably higher, ⁇ 60'. Preferably, it is preferably ⁇ 85 °C.
- polyolefin, polystyrene, butadiene rubber, natural rubber, polyisoprene rubber, styrene butadiene rubber, butyl rubber, ethylene propylene rubber and ternary can be used.
- One or more non-polar polymers such as ethylene propylene rubber, styrene-butadiene-styrene block copolymer and styrene-isoprene-styrene block copolymer as non-polar organic Film material.
- a certain amount of polar organic substance soluble in the high-barrier organic film layer material may be added to the high-barrier organic film layer, and the release period of the environmentally-friendly composite coated type slow-release fertilizer of the present invention can be freely adjusted by controlling the amount of the organic substance added thereto.
- adding wax-soluble additives with polar groups such as chlorinated paraffins, rosins and their esters, asphalt, etc. to paraffin; adding polar plasticizers such as dibutyl phthalate to non-polar polymers Classes, polyol esters, etc.
- the polar organic substance may be a polar low molecular weight organic substance (as exemplified above), or may be a polar prepolymer or a polymer such as an unsaturated polyester prepolymer added to the paraffin wax, which is crosslinked by coating.
- a polar low molecular weight organic substance as exemplified above
- a polar prepolymer or a polymer such as an unsaturated polyester prepolymer added to the paraffin wax, which is crosslinked by coating.
- water-soluble salts, starch, wood flour, plant chips, clay, talc, molecular sieve powder or bone powder to the high-barrier organic film layer can improve the permeability of the high-barrier organic film layer to water and fertilizer.
- the addition period can also adjust the release period of the environmentally friendly composite coated slow release fertilizer of the present invention.
- the sulfur film layer on the outer surface of the fertilizer core should be complete or substantially intact, and it is best not to have a large amount of damage, so the sulfur film layer should reach a certain average thickness.
- the average thickness of the sulfur film layer may be between l and 100/m, but it is preferably from 8 to 60 m.
- the total average thickness of the entire envelope should be able to bear the expansion force generated by the water swell of the fertilizer core, so that the overall envelope is broken, so the total average thickness of the envelope can be between 10 and 180 m.
- the total average thickness of the coating is preferably from 20 to 90 m, depending on the preferred average thickness of the sulfur film layer of from 8 to 60 m.
- the total average thickness of both the degradable polymer film layer and the sulfur-containing degradable polymer mixture film layer may be 5 to 180 m, but is preferably 8 to 50 m.
- the total average thickness of the high-barrier organic film layer may be 0 to 15 m, preferably 0 to 10/m.
- the average thickness of the outer layer of the sulfur film layer should not be less than 3 m, preferably not less than 5 // m.
- the total average thickness of the film layer of the sulfur-containing degradable polymer mixture and the total average thickness of the degradable polymer film layer may each be 0 100 / m, but the total average thickness of the film layer of the sulfur-containing degradable polymer mixture is 8 ⁇ 50 m is preferred, and the total average thickness of the degradable polymer film layer is preferably 0 to 35 m.
- the total average thickness of the envelope, the average thickness of the sulfur film layer, the total average thickness of both the degradable polymer film layer and the sulfur-containing degradable polymer mixture film layer, and the total average thickness of the sulfur-containing degradable polymer mixture film layer can be compared with the above The respective upper limit values are larger. The greater these thicknesses, the longer the release period of the environmentally friendly composite coated slow release fertilizer.
- the degradable polymer, the sulfur-containing degradable polymer and the ruthenium may be used.
- a surfactant is added to the coating liquid of the organic film layer.
- additives may be added to the sulfur film layer, the sulfur-containing degradable polymer mixture film layer, the degradable polymer film layer and the antimony-barrier organic film layer in the environmentally-friendly composite coated slow release fertilizer coating of the present invention.
- the additive is added for purposes such as further adjusting a certain property of each film layer or reducing cost.
- the environmentally friendly composite coated slow release urea of the present invention using urea as a fertilizer core is taken as an example to illustrate the specific implementation method and invention effect of the environmentally friendly composite coated slow release fertilizer of the present invention.
- the slow release property of the environmentally friendly composite coated slow release urea of the present invention is evaluated by the dissolution method in water.
- the dissolution method in water is the determination of the dissolution rate of urea in water in the environmentally friendly composite coated slow release urea of the present invention, and the specific method is as follows: 10 g
- the environmentally friendly composite coated slow release urea of the invention is immersed in 200 ml of water and immersed at a constant temperature of 25 ° C to measure the initial dissolution rate and the average differential dissolution rate.
- the initial dissolution rate ⁇ refers to the percentage of urea dissolved in the first 24 hours of immersion in the total mass of urea in the environmentally friendly composite coated slow release urea of the invention, and the average differential dissolution rate is 3 ⁇ 4 ⁇ from the soaking
- the average amount of urea dissolved per day from 2 days to 7 days is 10% of the total mass of urea in the environmentally-friendly composite coated slow-release urea of the present invention.
- the release period of the environmentally friendly composite coated slow release urea of the present invention in water is calculated (day):
- the granular industrial urea having a particle diameter of 2.0 to 4.0 mm is introduced into the fluidized bed coating device, and the granular urea is in a boiling state, and the temperature of the granular urea in the fluidized bed is maintained at 80 °C.
- the urea-formaldehyde resin prepolymer aqueous solution (urea resin prepolymer is urea: formaldehyde is prepared by reacting urea with formaldehyde in a molar ratio of 1:2) and molten sulfur at about 150 °C from two different nozzles simultaneously to granular urea.
- the surface is slowly sprayed, and by controlling the spray flow ratio thereof, the average mass fraction of sulfur in the formed sulfur-containing urea-formaldehyde resin mixture layer is 70%, and spraying until the formed layer of the sulfur-containing urea-formaldehyde resin mixture reaches the final product quality. 6% of the total mass of the environmentally-friendly composite coated slow-release urea, drying to remove water in the film.
- the urea-formaldehyde resin prepolymer is prepared by reacting urea with formaldehyde in a molar ratio of 1:1.6, and sulfur: urea-formaldehyde resin prepolymer.
- the mass ratio is 2:3) until the film quality of the layer containing the thiourea resin mixture is 6% of the total mass of the final product environmentally friendly composite coated slow release urea. Drying removes the film layer Water, and the urea-formaldehyde resin in the film layer is fully cured, that is, an environmentally friendly composite coated type slow-release urea is obtained.
- the release period of the prepared environmentally-friendly composite coated slow release urea was 145 days.
- the granular industrial urea having a particle diameter of 2.0 to 4.0 mm is introduced into the fluidized bed coating device, and the granular urea is in a boiling state, and the temperature of the granular urea in the fluidized bed is maintained at 90 °C.
- About 150 ⁇ of molten sulfur is slowly sprayed on the surface of the urea until the quality of the sulfur film reaches 7% of the total mass of the final product environmentally friendly composite coated slow release urea.
- a sulphur-containing melamine-formaldehyde resin prepolymer aqueous solution is sprayed on the surface of the sulfur film layer (melamine-formaldehyde resin prepolymer is prepared by reacting melamine with a molar ratio of 1:3 melamine and formaldehyde, sulfur: melamine one The mass ratio of the formaldehyde resin prepolymer is 7:3) until the film quality of the formed sulfur-containing melamine-formaldehyde resin mixture reaches 8% of the total mass of the final product environmentally friendly composite coated slow release urea.
- the water in the film layer is removed by drying, and the melamine-formaldehyde resin in the film layer is sufficiently cured to obtain an environmentally friendly composite coated type slow-release urea.
- the release period of the environmentally friendly composite coated slow release urea was 112 days.
- the granular industrial urea having a particle diameter of 2.0 to 4.0 mm is introduced into the fluidized bed coating device, and the granular urea is in a boiling state, and the temperature of the granular urea in the fluidized bed is maintained at 90 °C.
- Spraying a melamine-formaldehyde resin prepolymer aqueous solution (melamine-formaldehyde resin prepolymer is prepared by reacting melamine:melamine with a formaldehyde molar ratio of 1:4) onto formaldehyde, until the layer of melamine-formaldehyde resin film is formed.
- the layer quality reaches 2% of the total mass of the final finished environmentally friendly composite coated slow release urea, and the water is removed by drying. Then, molten sulphur of about 150 ° C is sprayed on the surface of the melamine-formaldehyde resin film layer until the quality of the formed sulfur film layer reaches 11% of the total mass of the final product environmentally friendly composite coated slow release urea. Finally, a melamine-formic acid resin prepolymer aqueous solution is sprayed on the surface of the sulfur film layer (the melamine-formic acid resin prepolymer is prepared by reacting melamine with a formaldehyde molar ratio of 1:3 and melamine) until the layer of melamine is formed.
- the quality of a formaldehyde resin film layer reaches 4% of the total quality of the final product environmentally friendly composite coated slow release urea.
- the water is removed from the film layer by drying, and the melamine-formaldehyde resin in the film layer is sufficiently cured to obtain an environmentally-friendly composite film-type slow-release urea.
- the release period of the environmentally-friendly composite membrane-type slow-release urea produced was 115 days.
- the granular industrial urea with a particle size of 2.0 ⁇ 4.0nm is added to the fluidized bed coating equipment, and the granular urea is in a boiling state.
- the temperature of the granular urea in the fluidized bed is maintained at 9 (TC.
- the molten sulfur is about 150 ° C slow. Slowly spray on the urea surface until the quality of the formed sulfur film reaches 16% of the total mass of the final product environmentally friendly composite coated slow release urea. Then, spray the melamine-formaldehyde resin prepolymer aqueous solution on the surface of the sulfur film (melamine one).
- the formaldehyde resin prepolymer is prepared by reacting melamine with a formaldehyde molar ratio of 1:2.7 in melamine and formaldehyde, until the quality of the formed melamine-formaldehyde resin film reaches the final quality of the final product environmentally friendly composite coated slow release urea. 4%.
- the water is removed from the film layer by drying, and the melamine-carboxylic acid resin in the film layer is sufficiently cured to obtain an environmentally-friendly composite film-type slow-release urea.
- the release period of the environmentally friendly composite coated slow release urea was 117 days.
- the granular industrial urea having a particle diameter of 2.0 to 4.0 mm is introduced into the fluidized bed coating device, and the granular urea is in a boiling state, and the temperature of the granular urea in the fluidized bed is maintained at 50 °C.
- the nitrocellulose solution (the solvent is a mixed solvent of ethanol, acetone and amyl acetate) and the molten sulfur at about 150 °C are simultaneously sprayed from the two different nozzles to the surface of the granular urea, respectively, by controlling their spraying.
- the flow ratio is such that the average mass fraction of sulfur in the formed sulfur-containing nitrocellulose mixture film layer is 80%, and the film quality of the layer of sulfur-containing nitrocellulose mixture formed until the final layer of the environmentally friendly composite coated type slow-release urea is reached. 6% of the total mass, dry to remove the solvent in the film. Then, stop spraying the nitrocellulose solution, and continue to spray 150 ° C molten sulfur on the surface of the sulfur-containing nitrocellulose mixture membrane layer until the quality of the formed sulfur film layer reaches the total quality of the final product environmentally friendly composite coated slow release urea. 8%.
- the nitrocellulose solution is sprayed on the surface of the sulfur film layer until the quality of the formed nitrocellulose film reaches 2% of the total mass of the final product environmentally friendly composite coated slow release urea.
- the solvent in the film layer is sufficiently dried to obtain an environmentally friendly composite coated type slow-release urea.
- the release period of the environmentally friendly composite coated slow release urea was 134 days.
- the granular industrial urea having a particle diameter of 2.0 to 4.0 mm is introduced into the fluidized bed coating device, and the granular urea is in a boiling state, and the temperature of the granular urea in the fluidized bed is maintained at 80 °C.
- Spraying a melamine-formaldehyde resin prepolymer aqueous solution (melamine-formaldehyde resin prepolymer is prepared by reacting melamine:melamine with a formaldehyde molar ratio of 1:3.5) with formaldehyde until the surface of the melamine-formaldehyde resin film is formed.
- the final product is 1.5% of the total mass of the environmentally-friendly composite coated slow-release urea, and the water is removed by drying. Then, about 150 ⁇ of molten sulfur is sprayed on the surface of the melamine-formaldehyde resin film layer until the quality of the formed sulfur film layer reaches 8% of the total mass of the final product environmentally friendly composite coated slow release urea. Finally, a melamine-formaldehyde resin prepolymer aqueous solution (melamine-formaldehyde resin prepolymer is prepared by reacting melamine:melamine with a molar ratio of 1:3 and formaldehyde) and 150 ⁇ of molten sulfur are respectively different from two groups.
- the nozzles are simultaneously sprayed onto the surface of the sulfur film layer, and by controlling the spray flow ratio thereof, the average mass fraction of sulfur in the formed sulfur-containing melamine-formaldehyde resin mixture layer is 80% until the formed layer of sulfur-containing melamine is formed.
- the film quality of the formaldehyde resin mixture reaches 7% of the total mass of the final product environmentally friendly composite coated slow release urea.
- the water is removed from the film layer by drying, and the melamine-formaldehyde resin in the film layer is sufficiently cured to obtain an environmentally-friendly composite film-type slow-release urea.
- the release period of the environmentally-friendly composite coated slow release urea was 118 days.
- the granular industrial urea having a particle diameter of 2.0 to 4.0 mm is introduced into the fluidized bed coating device, and the granular urea is in a boiling state, and the temperature of the granular urea in the fluidized bed is maintained at 90 °C.
- meltamine-formaldehyde resin prepolymer is prepared by reacting melamine: melamine with a formaldehyde molar ratio of 1:3 and formaldehyde, sulfur: melamine-formaldehyde resin prepolymer has a mass ratio of 4:1) sprayed on the urea surface, Until the formed layer of the sulfur-containing melamine-formaldehyde resin mixture has a film quality of 5% of the total mass of the final product environmentally friendly composite coated slow release urea, the water is removed by drying.
- a sulphur-containing melamine-formaldehyde resin prepolymer aqueous solution is sprayed on the surface of the sulfur film layer (melamine-formaldehyde resin prepolymer is prepared by reacting melamine with formaldehyde in a molar ratio of 1:3, and melamine: melamine The mass ratio of the waking resin prepolymer is 7:3) until the film quality of the layer of the sulfur-containing melamine-formaldehyde resin mixture formed reaches 3% of the total mass of the final product environmentally friendly composite coated slow release urea.
- a melamine-formaldehyde resin prepolymer aqueous solution is sprayed on the surface of the sulfur-containing melamine-formaldehyde resin mixture film layer
- melamine-formaldehyde resin prepolymer is prepared by reacting melamine with a molar ratio of melamine of formaldehyde: 1:1).
- the water is removed from the film layer by drying, and the melamine-formaldehyde resin in the film layer is sufficiently cured to obtain an environmentally friendly composite coated type slow-release urea.
- the release period of the prepared environmentally-friendly composite coated slow release urea was 146 days.
- the granular industrial urea having a particle diameter of 2.0 to 4.0 mm is introduced into the fluidized bed coating device, and the granular urea is in a boiling state, and the temperature of the granular urea in the fluidized bed is maintained at 90 °C.
- the molten sulfur at about 150 °C is slowly sprayed on the surface of the urea until the quality of the formed sulfur film reaches 9% of the total mass of the final product environmentally friendly composite coated slow release urea. Then, a sulfur-containing urea-formaldehyde resin prepolymer aqueous solution is sprayed on the surface of the sulfur film layer.
- the urea-formaldehyde resin prepolymer is prepared by reacting urea with formaldehyde in a molar ratio of 1:1.3, and sulfur: the quality of the urea-formaldehyde resin prepolymer. The ratio is 7:3) until the film quality of the formed sulfur-containing urea-formaldehyde resin mixture reaches 5% of the total mass of the final product environmentally friendly composite coated slow release urea.
- a urea-formaldehyde resin prepolymer aqueous solution is sprayed on the surface of the thiourea-containing resin mixture film layer (the urea-formaldehyde resin prepolymer is prepared by reacting urea with formaldehyde in a molar ratio of 1:1.8) until the urea-formaldehyde resin film is formed.
- the layer quality reaches 1.5% of the total quality of the finished product environmentally friendly composite coated slow release urea. Drying removes the water in the film layer and cures the urea-formaldehyde resin in the film layer sufficiently, that is, the environmentally friendly composite film-type slow-release urea is obtained.
- the release period of the environmentally friendly composite coated slow release urea was 105 days.
- the granular industrial urea having a particle diameter of 2.0 to 4.0 mm is introduced into the fluidized bed coating device, and the granular urea is in a boiling state, and the temperature of the granular urea in the fluidized bed is maintained at 70 °C.
- Tung oil and about 150 ⁇ of molten sulfur were sprayed from different nozzles simultaneously to the surface of granular urea.
- the average mass fraction of sulfur in the formed sulfur-containing tung oil resin mixture film layer was 70%. Spraying until the formation of the layer containing sulphur The film quality of the oleoresin mixture reaches 5% of the total mass of the final product environmentally friendly composite coated slow release urea.
- Granular industrial urea having a particle size of 2.0 to 4.0 mm is introduced into the fluidized bed coating apparatus, and the granular urea is in a boiling state, and the temperature of the granular urea in the fluidized bed is maintained at 75 °C.
- a sulphur-containing melamine-formaldehyde resin prepolymer aqueous solution (melamine-formaldehyde resin prepolymer is prepared by reacting melamine with formaldehyde in a molar ratio of 1:3.2, and sulfur: melamine-formaldehyde resin prepolymer) 7: 3) Sprayed on the urea surface until the formed layer of the sulfur-containing melamine-formic acid resin mixture has a film quality of 4% of the total mass of the final product environmentally friendly composite coated slow release urea, and the water is removed by drying.
- the surface of the sulfur-containing melamine-formaldehyde resin mixture film layer is slowly sprayed with molten sulfur at a temperature of about 150 ° C until the quality of the formed sulfur film layer reaches 6% of the total mass of the final product environmentally friendly composite coated slow release urea.
- the temperature of the granular urea in the fluidized bed is lowered to 60 ° C, and the paraffin wax (melting point 75 ° C) at a temperature of 90 ° C is sprayed on the surface of the sulfur film layer until the quality of the formed paraffin film layer reaches the final product environmentally friendly compound. 2% of the total mass of the coated slow release urea.
- tung oil (containing a drier of 0.4% tung oil) was sprayed on the surface of the paraffin layer until the quality of the tung oil resin film reached 2% of the total mass of the final product-encapsulated composite coated slow-release urea.
- the melamine-carboxylic acid resin and the tung oil resin in the film layer are sufficiently cured to obtain an environmentally-friendly composite film-type slow-release urea.
- the release period of the environmentally friendly composite coated slow release urea was 197 days.
- the granular industrial urea having a particle diameter of 2.0 to 4.0 mm is introduced into the fluidized bed coating device, and the granular urea is in a boiling state, and the temperature of the granular urea in the fluidized bed is maintained at 75 °C.
- a sulphur-containing melamine-formaldehyde resin prepolymer aqueous solution (melamine-formaldehyde resin prepolymer is prepared by reacting melamine with formaldehyde in a molar ratio of 1:3.2, and sulfur: melamine-formaldehyde resin prepolymer) 7: 3) Sprayed on the urea surface until the formed layer of the sulfur-containing melamine-formaldehyde resin mixture reaches 4% of the total mass of the final product environmentally friendly composite coated slow release urea, and the water is removed by drying.
- the surface of the film layer of the sulfur-containing melamine-formaldehyde resin mixture is slowly sprayed with molten sulfur at a temperature of about 150 ° C until the quality of the formed sulfur film layer reaches the final. 6% of the total quality of the finished environmentally friendly composite coated slow release urea.
- the temperature of the granular urea in the fluidized bed is lowered to 65 ° C, and the mixture of paraffin and rosin having a temperature of 95 ⁇ is sprayed (the mixture has a melting point of 80 ° C, and the paraffin: rosin mass ratio is 2:1). The melt is melted on the surface of the sulfur film layer.
- the surface of the paraffin and rosin mixture film was sprayed with tung oil (containing 0.4% of tung oil quality drier) until the quality of the tung oil resin film layer reached 2% of the total quality of the final product environmentally friendly composite coated slow release urea.
- tung oil containing 0.4% of tung oil quality drier
- the trimeric guanamine-formaldehyde resin and the tung oil resin in the film layer are fully cured, that is, the environmentally friendly composite coated type sustained-release urea is obtained.
- the release period of the prepared environmentally-friendly composite coated slow release urea was 158 days.
- the granular industrial urea having a particle diameter of 2.0 to 4.0 mm was placed in a drum coating apparatus controlled at a temperature of 75 ° C, and the rotating drum (rotation speed of 40 r/min) was caused to flow the granular urea in the drum.
- the solvent benzene was removed.
- the granular industrial urea having a particle diameter of 2.0 to 4.0 mm is introduced into the fluidized bed coating device, and the granular urea is in a boiling state, and the temperature of the granular urea in the fluidized bed is maintained at 70 °C.
- About 150 ⁇ of molten sulfur is slowly sprayed on the surface of the urea until the quality of the formed sulfur film reaches 9% of the total mass of the final product environmentally friendly composite coated slow release urea.
- styrene-butadiene-styrene block copolymer (SBS, grade raton D1101) cyclohexanide solution is sprayed on the surface of the sulfur film layer until the formed styrene-butadiene-styrene block copolymer
- SBS styrene-butadiene-styrene block copolymer
- the film quality reaches 1% of the total mass of the final product environmentally friendly composite coated slow release urea, and the solvent is sufficiently dried.
- a nitrocellulose solution (the solvent is a mixed solvent of ethanol, acetone and amyl acetate) is sprayed on the surface of the styrene-butadiene-styrene block copolymer film layer until the formed nitrocellulose film layer
- the quality reaches 3% of the total quality of the final finished environmentally friendly composite coated slow release urea.
- the solvent in the film layer is removed by drying to obtain an environmentally friendly composite coated slow release urea.
- the release period of the environmentally friendly composite coated slow release urea was 157 days.
- a sulphur-containing melamine-formaldehyde resin prepolymer aqueous solution (melamine-formaldehyde resin prepolymer is prepared by reacting melamine:melamine with a formaldehyde molar ratio of 1:2.7, and sulfur: melamine-formaldehyde resin prepolymer) Sprayed on the urea surface for 1:1) until the formed layer of the sulfur-containing melamine-formaldehyde resin mixture reaches 2% of the total mass of the final product environmentally friendly composite coated slow-release urea, and the water is removed by drying.
- the surface of the sulfur-containing melamine-formaldehyde resin mixture film layer is slowly sprayed with molten sulfur at a temperature of about 150 ° C until the quality of the formed sulfur film layer reaches 10% of the total mass of the final product environmentally friendly composite coated slow release urea.
- a sulphur-containing melamine-formaldehyde resin prepolymer aqueous solution is sprayed on the surface of the sulfur film layer (melamine-formaldehyde resin prepolymer is prepared by reacting melamine with formaldehyde in a molar ratio of 1:3, and melamine: melamine The mass ratio of the formaldehyde resin prepolymer is 2:3) until the film quality of the layer of the sulfur-containing melamine-formaldehyde resin mixture formed reaches 6% of the total mass of the final product environmentally friendly composite coated slow release urea.
- the water is removed from the film layer by drying, and the melamine-formaldehyde resin in the film layer is sufficiently cured to obtain an environmentally friendly composite coated type slow-release urea.
- the release period of the prepared environmentally-friendly composite coated slow release urea was 131 days.
- the granular industrial urea with a particle size of 2.0 ⁇ 4.0mm is added to the fluidized bed coating equipment, and the granular urea is in a boiling state, and the granular urea temperature in the fluidized bed is maintained at 90 ⁇ .
- urea resin prepolymer is prepared by reacting urea with formaldehyde in a molar ratio of 1:2, and formaldehyde: the mass ratio of sulfur: urea-formaldehyde resin prepolymer is 3 2), until the formed layer of the thiourea-containing resin mixture film layer reaches 6% of the total mass of the final product environmentally friendly composite coated type slow-release urea, and the water is removed by drying.
- molten sulfur at 150 ° C is slowly sprayed onto the surface of the film layer containing the thiourea resin mixture until the quality of the sulfur film layer formed reaches 10% of the total mass of the final product environmentally friendly composite coated slow release urea.
- a sulfur-containing urea-formaldehyde resin prepolymer aqueous solution is sprayed on the surface of the sulfur film layer (the urea-formaldehyde resin prepolymer is prepared by reacting urea with a formaldehyde molar ratio of 1:1.5 and formaldehyde, and sulfur: urea-formaldehyde resin prepolymer)
- the mass ratio is 1:3) until the film quality of the layer containing the thiourea resin mixture is 2% of the total mass of the final product environmentally friendly composite coated slow release urea.
- the water is removed from the film layer, and the urea-formaldehyde resin in the film layer is sufficiently cured to obtain an environmentally-friendly composite film-type slow-release urea.
- the release period of the environmentally friendly composite coated slow release urea was 115 days.
- the granular industrial urea having a particle diameter of 2.0 to 4.0 mm is introduced into the fluidized bed coating device, and the granular urea is in a boiling state, and the temperature of the granular urea in the fluidized bed is maintained at 80 °C.
- a melamine-formaldehyde resin prepolymer aqueous solution (melamine-formaldehyde resin prepolymer is prepared by reacting melamine: melamine with a formaldehyde molar ratio of 1:3) and about 150 ⁇ of molten sulfur from two different nozzles simultaneously The surface of the granular urea is slowly sprayed, and the sulfur content in the formed sulfur-containing melamine-formaldehyde resin mixture layer is controlled by controlling the spray flow ratio thereof.
- the average mass fraction of the sulfonate is 70% until the formed film layer of the sulfur-containing melamine-formaldehyde resin mixture reaches 3% of the total mass of the final product environmentally friendly composite coated slow release urea, and the water is removed by drying. Then, stop spraying the melamine-formaldehyde resin prepolymer aqueous solution, and continue to spray the molten sulfur at a temperature of about 150 ° C on the surface of the sulfur-containing melamine-formaldehyde resin mixture film layer until the quality of the formed sulfur film layer reaches the final product environmentally friendly composite coating type. 3.5% of the total mass of slow release urea.
- a sulphur-containing melamine-formaldehyde resin prepolymer aqueous solution is sprayed on the surface of the sulfur film layer (melamine-formaldehyde resin prepolymer is prepared by reacting melamine with formaldehyde in a molar ratio of 1:3, and melamine: melamine The mass ratio of the formaldehyde resin prepolymer is 1:1) until the film quality of the layer of the sulfur-containing triazide-formaldehyde resin mixture formed reaches 2% of the total mass of the final product environmentally friendly composite coated slow release urea.
- the melamine-formaldehyde resin in the film layer is sufficiently dried by sufficiently drying to remove water in the film layer, thereby obtaining an environmentally friendly composite coated type slow-release urea.
- the release period of the environmentally friendly composite coated slow release urea prepared was 56 days.
- Granular industrial urea having a particle size of 2.0 to 4.0 mm is introduced into the fluidized bed coating apparatus, and the granular urea is in a boiling state, and the temperature of the granular urea in the fluidized bed is maintained at 90 °C.
- About 150 ⁇ of molten sulfur is slowly sprayed on the surface of the urea until the quality of the sulfur film reaches 10% of the total mass of the final product environmentally friendly composite coated slow release urea.
- a sulphur-containing melamine-formaldehyde resin prepolymer aqueous solution is sprayed on the sulfur film layer (melamine-formaldehyde resin prepolymer is prepared by reacting melamine with a formaldehyde molar ratio of 1:3, and melamine: melamine-formaldehyde
- the mass ratio of the resin prepolymer is 3: 2) until the film quality of the formed sulfur-containing melamine-formaldehyde resin mixture reaches 4% of the total mass of the final product environmentally friendly composite coated slow release urea.
- the water is removed from the film layer, and the melamine-formaldehyde resin in the film layer is sufficiently cured to obtain an environmentally-friendly composite film-type slow-release urea.
- the release period of the environmentally friendly composite coated slow release urea was 75 days.
- the granular industrial urea with a particle size of 2.0 ⁇ 4.0mm is added to the fluidized bed coating equipment, and the granular urea is in a boiling state, and the granular urea temperature in the fluidized bed is maintained at 70T:.
- a sulphur-containing melamine-formaldehyde resin prepolymer aqueous solution (melamine-formaldehyde resin prepolymer is prepared by reacting melamine: melamine having a molar ratio of 1:3 with formaldehyde, sulfur: melamine-formaldehyde resin prepolymer mass ratio 7: 3) Sprayed on the urea surface until the formed layer of the sulfur-containing melamine-formaldehyde resin mixture reaches 4% of the total mass of the final product environmentally friendly composite coated slow release urea, and the water is removed by drying.
- the surface of the sulfur-containing melamine-formaldehyde resin mixture film layer is slowly sprayed with molten sulfur at a temperature of about 150 ° C until the quality of the formed sulfur film layer reaches 6% of the total mass of the final product environmentally friendly composite coated slow release urea.
- a benzene solution of acrylonitrile-butadiene-styrene copolymer (Lanzhou Petrochemical Company, brand ABS-301) is sprayed on the surface of the sulfur film layer until the formed acrylonitrile-butadiene-styrene copolymer film
- the layer quality reaches the total quality of the final product environmentally friendly composite coated slow release urea 1%.
- the surface of the acrylonitrile-butadiene-styrene copolymer film was sprayed with tung oil (containing 0.4% dregs of tung oil) until the quality of the tung oil resin film reached the final product environmentally friendly composite film type sustained release. 2% of the total mass of urea.
- the melamine-formaldehyde resin and the tung oil resin in the film layer are fully cured, that is, the environmentally-friendly composite coated type slow-release urea is obtained.
- the release period of the environmentally friendly composite coated slow release urea was 165 days.
- the granular industrial urea with a particle size of 2.0 to 4.0 min is added to the fluidized bed coating equipment, and the granular urea is in a boiling state, and the temperature of the granular urea in the fluidized bed is maintained at 90 °C.
- the melamine-formaldehyde resin prepolymer aqueous solution (melamine-formaldehyde resin prepolymer is prepared by reacting melamine:melamine with a formaldehyde molar ratio of 1:3.5 and formaldehyde) is slowly sprayed on the surface of the granular urea until the layer of melamine is formed.
- the quality of the formaldehyde resin film layer reaches 1.5% of the total quality of the final product environmentally friendly composite coated slow release urea. Then, the melamine-formaldehyde resin prepolymer aqueous solution is sprayed slowly from the two different nozzles to the surface of the melamine-formaldehyde resin film layer (melamine-formaldehyde resin prepolymer is melamine: melamine with a molar ratio of 1:2.5)
- the formaldehyde produced by the formaldehyde reaction and the molten sulfur at about 150 ° C, by controlling the spray flow ratio thereof, the average mass fraction of sulfur in the formed sulfur-containing melamine-formaldehyde resin mixture layer is 85%, and spraying until the layer is formed.
- the film quality of the sulfur-containing melamine-formaldehyde resin mixture reaches 4% of the total mass of the final product environmentally friendly composite coated slow release urea, and the water is removed by drying. Subsequently, the spraying of the melamine-formaldehyde resin prepolymer aqueous solution is stopped, and the molten sulfur is continuously sprayed at about 150 ° C until the quality of the formed sulfur film layer reaches 6% of the total mass of the final product environmentally friendly composite coated slow release urea.
- a sulphur-containing melamine-formaldehyde resin prepolymer aqueous solution is sprayed on the surface of the sulfur film layer (melamine-formaldehyde resin prepolymer is prepared by reacting melamine: melamine having a molar ratio of 1:3 with formaldehyde, sulfur: melamine one The mass ratio of the formaldehyde resin prepolymer is 7:3) until the film quality of the layer of the sulfur-containing melamine-formaldehyde resin mixture formed reaches 3% of the total mass of the final product environmentally friendly composite coated slow release urea.
- a melamine-formaldehyde resin prepolymer aqueous solution is slowly sprayed on the surface of the sulfur-containing melamine-formaldehyde resin mixture film layer (melamine-formaldehyde resin prepolymer is prepared by reacting melamine with a formaldehyde molar ratio of 1:2 and formaldehyde). ), until the formation of the layer of melamine-formic acid resin film layer quality reached 1.5% of the total quality of the final product environmentally friendly composite coated slow release urea.
- the water is removed from the film layer by drying, and the melamine-formaldehyde resin in the film layer is sufficiently cured to obtain an environmentally friendly composite coated type slow-release urea.
- the release period of the environmentally friendly composite coated slow release urea was 156 days.
- a melamine-formaldehyde resin prepolymer aqueous solution (melamine-formaldehyde resin prepolymer is prepared by reacting melamine with a formaldehyde molar ratio of 1:2.6 and melamine) and a sulphur sulphur at a temperature of about 150 ° C are respectively different from the two groups. The nozzle is slowly sprayed onto the surface of the flaky urea at the same time.
- Their spraying flow ratio is such that the average mass fraction of sulfur in the formed sulfur-containing melamine-formaldehyde resin mixture layer is 70%, and the quality of the layer of the sulfur-containing melamine-formaldehyde resin mixture formed until the formation reaches the final finished environmentally friendly composite package. 5% of the total mass of the membrane type slow-release urea, drying to remove water in the film layer. Then, stop spraying the melamine-formaldehyde resin prepolymer aqueous solution, and continue to spray 150 ° C molten sulfur on the surface of the sulfur-containing melamine-formaldehyde resin mixture film layer until the quality of the formed sulfur film layer reaches the final product environmentally friendly composite coating type. Release 15% of the total quality of urea.
- a sulphur-containing melamine-formaldehyde resin prepolymer aqueous solution is sprayed on the surface of the sulfur film layer (melamine-formaldehyde resin prepolymer is prepared by reacting melamine with formaldehyde in a molar ratio of 1:3, and melamine: melamine The mass ratio of the formaldehyde resin prepolymer is 1:1) until the film quality of the layer of the sulfur-containing melamine-formaldehyde resin mixture formed reaches 5% of the total mass of the final product environmentally friendly composite coated slow release urea.
- the water is removed from the film layer by drying, and the melamine-formaldehyde resin in the film layer is sufficiently cured to obtain an environmentally friendly composite coated type slow-release urea.
- the release period of the prepared environmentally-friendly composite coated slow release urea was 245 days.
- the granular industrial urea with a particle size of 2.0 to 4.0 mm was placed in a drum coating device with a temperature control of 65 ° C, and the rotating drum (rotation speed 40 r / min) was used to flow the granular urea in the drum.
- Spraying a solution of polyvinyl formal resin (polyvinyl alcohol grade 1799, acetal degree 55%) on the surface of granular urea until the formed polyvinyl formal resin film layer The quality reaches 3% of the total mass of the final product environmentally friendly composite coated slow release urea, and the solvent is sufficiently dried.
- the granular industrial urea with a particle size of 2.0 ⁇ 4.0imn is added to the fluidized bed coating equipment, and the granular urea is in a boiling state, and the granular urea temperature in the fluidized bed is maintained at 90 °C.
- the aqueous solution of the melamine-modified urea-formaldehyde resin prepolymer is slowly sprayed on the surface of the granular urea until the quality of the layer of the melamine-modified urea-formaldehyde resin layer reaches 2% of the total mass of the final product environmentally friendly composite coated slow-release urea.
- the polyvinyl alcohol-modified urea-formaldehyde resin prepolymer aqueous solution and 150 ⁇ of molten sulfur are sprayed on the surface of the melamine-modified urea-formaldehyde resin film layer simultaneously, and the spray flow ratio is controlled by controlling the spray flow ratio thereof.
- the average mass fraction of sulfur in the film layer of the sulfur-containing polyvinyl alcohol modified urea-formaldehyde resin mixture is 75%, and the quality of the film layer of the sulfur-containing polyvinyl alcohol-modified urea-formaldehyde resin mixture formed until the formation of the layer is the final product environmentally friendly composite film type Release 3% of the total mass of urea, dry to remove water in the film.
- the spraying of the polyvinyl alcohol-modified urea-formaldehyde resin prepolymer aqueous solution is stopped, and the molten sulfur is continuously sprayed for about 150 C until the quality of the formed sulfur film layer reaches 7% of the total mass of the final product environmentally friendly composite coated slow-release urea.
- the ethanol-modified melamine-formaldehyde resin prepolymer aqueous solution and the molten sulfur at about 150 °C are sprayed slowly onto the surface of the sulfur film layer, and the sulfur content formed is controlled by controlling the spray flow ratio thereof.
- the average mass fraction of sulfur in the membrane of the ethanol-modified melamine-formaldehyde resin mixture is 65%, and the quality of the film layer of the melamine-modified melamine-formaldehyde resin mixture is reached until the final product of the environmentally friendly composite coating type slow-release urea is formed. 2% of the total mass.
- the melamine-formaldehyde resin prepolymer aqueous solution is slowly sprayed on the surface of the thiol-modified melamine-formaldehyde resin mixture film layer (melamine-formaldehyde resin prepolymer is melamine: melamine and formaldehyde with a molar ratio of 1:1.5)
- the reaction is prepared) until the quality of the layer of the melamine-formaldehyde resin layer formed reaches 2% of the total mass of the final product environmentally friendly composite coated slow release urea.
- the water in the film layer is removed by drying, and the modified urea-formaldehyde resin and the (modified) melamine-formaldehyde resin in the film layer are sufficiently cured to obtain an environmentally-friendly composite film-type slow-release urea.
- the release period of the environmentally friendly composite coated slow release urea prepared was 160 days.
- the granular industrial urea having a particle diameter of 2.0 to 4.0 mm is introduced into the fluidized bed coating device, and the granular urea is in a boiling state, and the temperature of the granular urea in the fluidized bed is maintained at 90 °C.
- the n-butanol-modified urethane resin prepolymer aqueous solution and the molten sulfur at about 150 °C are simultaneously sprayed from the two different nozzles to the urea surface, and the formed sulfur-containing n-butanol is changed by controlling the spray flow ratio thereof.
- the average mass fraction of sulfur in the film layer of the urea-formaldehyde resin mixture is 80%, and the film quality of the layer of sulfur-containing n-butanol-modified urea-formaldehyde resin mixture is up to 4, which is the total quality of the final product environmentally friendly composite coated type slow-release urea. %, dried to remove water in the film layer. Subsequently, the surface of the sulfur-containing n-butanol-modified urea-formaldehyde resin mixture film layer was slowly sprayed with molten sulfur at a temperature of about 150 ° C until the quality of the formed sulfur film layer reached 6% of the total mass of the final product environmentally friendly composite coated slow release urea.
- a sulfur-containing ethanol-polyvinyl alcohol-modified melamine-formaldehyde resin prepolymer aqueous solution is sprayed on the surface of the sulfur film layer (the mass ratio of sulfur:ethanol-polyvinyl alcohol modified melamine-formaldehyde resin prepolymer is 7: 3), until the formation of the layer of sulfur-containing ethanol-polyvinyl alcohol modified melamine-formaldehyde resin mixture film layer quality reached 4% of the total quality of the final product environmentally friendly composite coated slow release urea.
- urea-formaldehyde resin prepolymer aqueous solution is sprayed on the surface of the thiol-polyvinyl alcohol-modified melamine-formaldehyde resin mixture film layer (urea resin prepolymer is urea: formaldehyde molar ratio of 1:1.05 urea and formaldehyde reaction Prepared) until the quality of the layer of urea-formaldehyde resin film formed reaches 1% of the total mass of the final product environmentally friendly composite coated slow release urea.
- the water in the film layer is removed by drying, and the (modified) urea-formaldehyde resin and the modified melamine-formaldehyde resin in the film layer are sufficiently cured to obtain an environmentally friendly composite coated type slow-release urea.
- the release period of the environmentally friendly composite coated slow release urea was 142 days.
- the urea-formaldehyde resin prepolymer aqueous solution is prepared by reacting urea with formaldehyde, and the molar ratio of urea to formaldehyde may be in the range of 1: (1 ⁇ 3), which is generally known by those skilled in the art, usually 1 : ( 1 ⁇ 2)
- a 2% ammonium chloride curing agent having a urea resin resin prepolymer mass of 2% is added before the film coating.
- the melamine modified urea-formaldehyde resin prepolymer aqueous solution is prepared by the reaction of urea, melamine and formaldehyde.
- the urea:melamine:formaldehyde molar ratio is 1:1:4, and the melamine modified urea-formaldehyde resin prepolymer is added with 2% of the chlorine before the coating.
- Ammonium curing agent The aqueous solution of polyvinyl alcohol modified urea-formaldehyde resin prepolymer is prepared by reacting urea, formaldehyde and polyvinyl alcohol. The ratio of urea:formaldehyde:polyvinyl alcohol (1799) is 100:89:3, and polyvinyl alcohol is added before coating.
- the urea-formaldehyde resin prepolymer has a 2% ammonium chloride curing agent.
- n-butanol modified urea-formaldehyde resin prepolymer aqueous solution is prepared by the reaction of urea, formaldehyde and n-butanol.
- the urea:formaldehyde: n-butanol molar ratio is 1: 1.37: 1, and the n-butanol modified urea-formaldehyde resin is added before the film coating.
- the aqueous solution of the melamine-formaldehyde resin prepolymer is prepared by reacting melamine with formaldehyde, and the molar ratio of melamine to formaldehyde may be in the range of 1: (1 ⁇ 4), which is generally known to those skilled in the art, usually It is preferred to use 1: (1.5 ⁇ 3.5), and add 2% ammonium chloride or triethanolammonium curing agent of melamine-formaldehyde resin prepolymer before coating.
- the ethanol modified melamine-formaldehyde resin prepolymer aqueous solution is prepared by the reaction of trimeric amine, formaldehyde and ethanol.
- the melamine:formaldehyde:ethanol molar ratio is 1:2.5:2, and the ethanol modified melamine-formaldehyde resin is pre-coated before coating. 2% ammonium chloride curing agent.
- the ethanol-polyvinyl alcohol modified melamine-formaldehyde resin prepolymer aqueous solution is prepared by the reaction of melamine, formaldehyde, ethanol and polyvinyl alcohol, and the melamine:formaldehyde:ethanol:polyvinyl alcohol (1788) mass ratio is 100:67:12: 2.5, before the film coating, add ethanol-polyvinyl alcohol modified melamine-formaldehyde resin prepolymer mass 2% ammonium chloride curing agent.
- the modified urea-formaldehyde resin and the modified melamine-formaldehyde resin are respectively a urea-formaldehyde resin and a melamine-formaldehyde resin
- the modified urea-formaldehyde resin and the modified melamine used in the above embodiments are
- the formaldehyde resin is only a representative of the modified urea 'aldehyde resin and the modified melamine-formaldehyde resin respectively.
- the preparation formula of the modified urethane resin and the modified melamine-formaldehyde resin can only be used as a formula, and The scope of the invention is not limited.
- the melamine resin in the amino resin may be prepared by using glyoxal and furfural instead of formaldehyde in addition to the above (modified) melamine-formaldehyde resin, and the related embodiments are not listed in the detailed description of the present specification, but such a class Melamine resins are still within the scope of the invention.
- the tung oil used for the tanning is a commercially available tung oil from Qiubei, Yunnan, having an acid value of 5.0 mgKOH/g.
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Abstract
Description
环保复合包膜型缓释肥料 Environmentally friendly composite coated slow release fertilizer
技术领域 Technical field
本发明涉及一种包膜型缓释肥料, 特别涉及一种环保复合包膜型缓释肥料, 属于 肥料工业领域。 The invention relates to a coated slow release fertilizer, in particular to an environmentally friendly composite coated slow release fertilizer, belonging to the field of fertilizer industry.
背景技术 Background technique
目前, 缓释肥料是世界肥料工业的发展方向。 其中, 包膜型缓释肥料是缓释肥料 的发展重点, 但不可降解包膜型缓释肥料的包膜遗留在环境中将会对环境产生污染, 因此,幵发可降解包膜的环保包膜型缓释肥料符合环境保护和社会可持续发展的要求, 将成为今后缓释肥料的主流。 At present, slow release fertilizer is the development direction of the world fertilizer industry. Among them, coated slow release fertilizer is the development focus of slow release fertilizer, but the envelope of non-degradable coated slow release fertilizer will be polluted by the environment, so the environmental protection package of degradable envelope is developed. Membrane slow release fertilizer meets the requirements of environmental protection and social sustainable development, and will become the mainstream of slow release fertilizer in the future.
但是可降解材料的透水和透肥速度都很大, 因此制备得到的可降解包膜型缓释肥 料的释放期都很短, 一般只有几天, 比如采用脲醛树脂包膜的包膜型缓释肥料和木质 素改性物包膜的包膜型缓释肥料。 提高释放期是可降解包膜型缓释肥料需要解决的难 题, 也是可降解包膜型缓释肥料未来可以实用化的关键。 , However, the degradable material has a high permeable and transdermal speed, so the release period of the prepared degradable coated slow-release fertilizer is very short, generally only a few days, such as the sustained release of the envelope type using a urea-formaldehyde resin coating. A coated slow release fertilizer coated with fertilizer and lignin modified material. Increasing the release period is a difficult problem to be solved for the degradable coated slow release fertilizer, and it is also the key to the practical application of the degradable coated slow release fertilizer in the future. ,
发明内容 Summary of the invention
本发明的目的在于提供一种释放期较长的、 包膜材料完全或几乎完全可降解的环 保复合包膜型缓释肥料。 SUMMARY OF THE INVENTION It is an object of the present invention to provide an environmentally-protected composite coated slow release fertilizer which has a long release period and which is completely or almost completely degradable.
实现本发明目的的技术解决方案为: 一种环保复合包膜型缓释肥料, 由肥料芯和 肥料芯外面的包膜组成, 包膜包含: (a)硫磺膜层, (b)含硫可降解聚合物混合物膜 层和 /或可降解聚合物膜层, 有或无(c) 高阻透有机膜层; 其中, 硫磺膜层是整个包 膜的里层或中间层。 The technical solution for achieving the object of the present invention is: an environmentally friendly composite coated slow release fertilizer consisting of a fertilizer core and a coating on the outer side of the fertilizer core, the envelope comprising: (a) a sulfur film layer, (b) a sulfur-containing film Degrading the polymer mixture film layer and/or the degradable polymer film layer, with or without (c) a high barrier organic film layer; wherein the sulfur film layer is the inner or intermediate layer of the entire envelope.
本发明环保复合包膜型缓释肥料的含硫可降解聚合物混合物膜层中, 硫磺的平均 质量分数可以为 0%~95%, 优选为 20%~90%。 In the film of the sulfur-containing degradable polymer mixture of the environmentally friendly composite coated slow release fertilizer of the present invention, the average mass fraction of sulfur may be 0% to 95%, preferably 20% to 90%.
本发明环保复合包膜型缓释肥料中釆用的可降解聚合物为非水溶性的可降解聚合 物, 可以是氨基树脂、 聚乙烯醇及其共聚物的缩醛树脂、 不饱和油树脂和天然聚合物 及其衍生物等中的一种或一种以上。其中, 天然聚合物及其衍生物可以是硝酸纤维素、 紫胶、 醋酸纤维素、 交联淀粉、 甲壳素衍生物、 木质素衍生物等中的一种或一种以上。 The degradable polymer used in the environmentally friendly composite coated slow release fertilizer of the invention is a water-insoluble degradable polymer, and may be an amino resin, an acetal resin of polyvinyl alcohol and a copolymer thereof, an unsaturated oleoresin and One or more of natural polymers and derivatives thereof. Among them, the natural polymer and the derivative thereof may be one or more of nitrocellulose, shellac, cellulose acetate, crosslinked starch, chitin derivative, lignin derivative, and the like.
本发明环保复合包膜型缓释肥料包膜中的高阻透有机膜层最好为非极性有机膜 层。 非极性有机膜层的材料可以是非极性低分子量有机物和 /或非极性聚合物, 其中 非极性有机膜层以仅采用非极性低分子量有机物为优选。 非极性有机膜层以紧贴硫磺 膜层为优选, 并且非极性有机膜层最好不是包膜的最外膜层。 非极性低分子量有机物 可以是熔点 40°C的蜡、熔点或软化点 40°C且分子量≤2000的聚烯烃或聚苯乙烯以及 软化点 40Ό的石油树脂等中的一种或一种以上。 非极性聚合物可以是聚烯烃、 聚苯 乙烯、 顺丁橡胶、 天然橡胶、 聚异戊二烯橡胶、 丁苯橡胶、 丁基橡胶、 乙丙橡胶及三 元乙丙橡胶、 苯乙烯一丁二烯一苯乙烯嵌段共聚物和苯乙烯一异戊二烯一苯乙烯嵌段 共聚物等中的一种或一种以上。 The high barrier organic film layer in the environmentally friendly composite coated slow release fertilizer coating of the present invention is preferably a non-polar organic film layer. The material of the non-polar organic film layer may be a non-polar low molecular weight organic substance and/or a non-polar polymer, wherein the non-polar organic film layer is preferably a non-polar low molecular weight organic substance. The non-polar organic film layer is preferably adhered to the sulfur film layer, and the non-polar organic film layer is preferably not the outermost film layer of the envelope. The non-polar low molecular weight organic substance may be one or more of a wax having a melting point of 40 ° C, a melting point or a softening point of 40 ° C and a polyolefin or polystyrene having a molecular weight of ≤2000 and a petroleum resin having a softening point of 40 Å. The non-polar polymer may be a polyolefin or a polyphenylene Ethylene, butadiene rubber, natural rubber, polyisoprene rubber, styrene butadiene rubber, butyl rubber, ethylene propylene rubber and ethylene propylene diene rubber, styrene butadiene styrene block copolymer and styrene One or more of an isoprene-styrene block copolymer and the like.
本发明环保复合包膜型缓释肥料的高阻透有机膜层中可以含有缓释调节剂。 缓释 调节剂以可溶于高阻透有机膜层材料的极性有机物为优选。 The high barrier organic film layer of the environmentally friendly composite coated slow release fertilizer of the present invention may contain a sustained release modifier. The sustained release modifier is preferably a polar organic substance which is soluble in the material of the high barrier organic film layer.
本发明环保复合包膜型缓释肥料, 包膜总平均厚度可以为 10~180 ^ m, 其中硫磺 膜层的平均厚度可以为 l~100 m,可降解聚合物膜层和含硫可降解聚合物混合物膜层 两者的总平均厚度可以为 5~180 / m, 高阻透有机膜层的总平均厚度可以为 0~15 m, 硫磺膜层往外的膜层平均厚度不低于 3 m;含硫可降解聚合物混合物膜层的总平均厚 度为 0~100 m, 可降解聚合物膜层的总平均厚度为 0~100 m。 The environmentally friendly composite coated slow-release fertilizer of the invention has a total average thickness of 10~180 ^ m, wherein the average thickness of the sulfur film layer can be from 1 to 100 m, the degradable polymer film layer and the sulfur-containing degradable polymerization layer. The total average thickness of the film mixture layer may be 5 to 180 / m, the total average thickness of the high barrier organic film layer may be 0 to 15 m, and the average thickness of the outer layer of the sulfur film layer is not less than 3 m; The total average thickness of the sulfur-containing degradable polymer mixture film layer is 0 to 100 m, and the total average thickness of the degradable polymer film layer is 0 to 100 m.
其中,包膜总平均厚度以 20~90 m为优选,其中硫磺膜层的平均厚度以 8~60/ m 为优选, 可降解聚合物膜层和含硫可降解聚合物混合物膜层两者的总平均厚度以 8~50/ m为优选, 高阻透有机膜层的总平均厚度以 0~10/ m为优选, 硫磺膜层往外的 膜层平均厚度最好不低于 5 / m; 含硫可降解聚合物混合物膜层的总平均厚度以 8-50 μ 为优选, 可降解聚合物膜层的总平均厚度以 0~35 μ m为优选。 Wherein, the total average thickness of the coating is preferably from 20 to 90 m, wherein the average thickness of the sulfur film layer is preferably from 8 to 60/m, and both the degradable polymer film layer and the sulfur-containing degradable polymer mixture film layer are The total average thickness is preferably 8~50/m, the total average thickness of the high barrier organic film layer is preferably 0~10/m, and the average thickness of the outer layer of the sulfur film layer is preferably not less than 5/m; The total average thickness of the film layer of the sulfur degradable polymer mixture is preferably from 8 to 50 μ, and the total average thickness of the degradable polymer film layer is preferably from 0 to 35 μm.
本发明环保复合包膜型缓释肥料釆用可降解聚合物与硫磺作为全部或主要包膜材 料, 全部包膜材料对环境无污染或污染很小, 因此是完全或几乎完全环保型缓释肥料; 当包膜中没有复合非极性聚合物膜层时, 是完全环保型缓释肥料。 The environmental protection composite coated slow release fertilizer of the invention uses degradable polymer and sulfur as all or main coating materials, and all the coating materials have no pollution to the environment or little pollution, so it is a completely or almost completely environmentally friendly slow release fertilizer. When the coating has no composite non-polar polymer film layer, it is a completely environmentally friendly slow-release fertilizer.
本发明环保复合包膜型缓释肥料采用可降解聚合物膜层和 /或含硫可降解聚合物 混合物膜层与硫磺膜层复合, 由于硫磺膜层对水和肥料的阻透性高, 同时由于可降解 聚合物是非水溶性的, 在肥料施入田土中不会遇水溶去, 其可降解聚合物膜层和 /或 含硫可降解聚合物混合物膜层在整个使用过程中可以一直发挥包膜阻透作用, 因此釆 用可降解聚合物作为包膜材料的本发明可降解包膜型缓释肥料可以具有较长的释放 期。 同时, 由于硫磺的价格比肥料还低, 因此本发明环保复合包膜型缓释肥料的成本 可以较低。 特别是, 脲醛树脂和三聚氰胺 -甲醛树脂是比较价廉的可降解聚合物, 比普 通的难降解聚合物的价格都低得多, 而且它们本身是缓释氮肥, 脲醛树脂和三聚氰胺- 甲醛树脂的含氮量分别约为 30%和 54%,三聚氰胺-甲醛树脂的含氮量比尿素的含氮量 (约 45%)还高, 因此以脲酸树脂和三聚氰胺 -甲醛树脂为包膜材料的本发明环保复合 包膜型缓释肥料是完全以肥包肥型缓释肥料, 肥分很高, 成本低。 比如, 按照纯肥料 的成本指数为 100计, 则硫磺的成本指数约为 50,脲醛树脂和三聚氰胺-甲醛树脂的成 本指数分别约为 450和 600, 以肥料 85%、 硫磺 10%和脲酲树脂或三聚氰胺-甲醛树脂 5%组成的本发明环保复合包膜型缓释肥料为例计算, 则它们的总成本指数分别约为 112.5和 120, 只比纯肥料成本高 12.5%~20%, 完全可以用作普通的农业田地用肥。 特别是, 本发明环保复合包膜型缓释肥料采用含硫可降解聚合物混合物膜层与硫 磺膜层复合时, 含硫可降解聚合物混合物膜层对水和肥料的阻透性比单纯可降解聚合 物膜层强, 特别是其中的含硫量髙(比如 80%〜90%) 时, 对水和肥料的阻透性较强, 因此包膜中有含硫可降解聚合物混合物膜层的本发明环保复合包膜型缓释肥料的释放 期更长, 特别是含硫可降解聚合物混合物膜层紧贴硫磺膜层时。 同时, 在达到有效保 护硫磺膜层的情况下, 采用含硫可降解聚合物混合物膜层可以进一步减少可降解聚合 物的用量, 成本更低。 The environmentally friendly composite coated slow release fertilizer of the invention is combined with a sulfur film layer by using a degradable polymer film layer and/or a sulfur-containing degradable polymer mixture film layer, because the sulfur film layer has high barrier to water and fertilizer, and at the same time Since the degradable polymer is water-insoluble, it does not dissolve in the soil when the fertilizer is applied to the soil, and the degradable polymer film layer and/or the sulfur-containing degradable polymer mixture film layer can always be used throughout the use process. The membrane barrier effect, and thus the degradable coated slow release fertilizer of the present invention using a degradable polymer as a coating material can have a long release period. At the same time, since the price of sulfur is lower than that of the fertilizer, the cost of the environmentally friendly composite coated slow release fertilizer of the present invention can be low. In particular, urea-formaldehyde resins and melamine-formaldehyde resins are relatively inexpensive degradable polymers, which are much cheaper than conventional refractory polymers, and which are themselves slow-release nitrogen fertilizers, urea-formaldehyde resins and melamine-formaldehyde resins. The nitrogen content is about 30% and 54% respectively, and the nitrogen content of the melamine-formaldehyde resin is higher than the nitrogen content of urea (about 45%). Therefore, the urethane resin and the melamine-formaldehyde resin are used as the coating material. The invention relates to an environmentally-friendly composite coated slow-release fertilizer which is completely fertilizer-fermented slow-release fertilizer with high fertilizer content and low cost. For example, according to the cost index of pure fertilizer, the cost index of sulfur is about 50, the cost index of urea-formaldehyde resin and melamine-formaldehyde resin is about 450 and 600, respectively, 85% of fertilizer, 10% of sulfur and urethane resin. Or the 5% melamine-formaldehyde resin composition of the environmentally friendly composite coated slow release fertilizer of the present invention is calculated as an example, and their total cost index is about 112.5 and 120, only 12.5%~20% higher than the cost of pure fertilizer, can be used as a common agricultural field fertilizer. In particular, when the environmentally friendly composite coated slow release fertilizer of the present invention is combined with a sulfur film layer by a sulfur-containing degradable polymer mixture film layer, the barrier property of the sulfur-containing degradable polymer mixture film to water and fertilizer is simpler than The degradable polymer film layer is strong, especially when the sulfur content is 髙 (such as 80%~90%), the barrier property to water and fertilizer is strong, so there is a film layer of sulfur-containing degradable polymer mixture in the coating film. The environmentally friendly composite coated slow release fertilizer of the invention has a longer release period, especially when the sulfur-containing degradable polymer mixture film layer is in close contact with the sulfur film layer. At the same time, in the case of effectively protecting the sulfur film layer, the use of the sulfur-containing degradable polymer mixture film layer can further reduce the amount of the degradable polymer, and the cost is lower.
如果在本发明环保复合包膜型缓释肥料的包膜中, 再复合很薄的高阻透有机膜层 (用量很小, 比能单独保护硫磺膜层的用量小) 的话, 可以使本发明环保复合包膜型 缓释肥料的释放期进一步明显延长, 特别是当高阻透有机膜层为非极性有机膜层, 且 非极性有机膜层紧贴硫磺膜层时, 其效果明显。 因此, 包膜中复合有非极性有机膜层 的本发明环保复合包膜型缓释肥料的释放期可以很长。 并且, 在高阻透有机膜层中加 入可溶于高阻透有机膜层材料的极性有机物或其它缓释调节剂, 通过控制加入量可以 很自由地调节释放期, 比采用改变包膜膜层总厚度调节释放期的方法更有效并且更经 济。特别是,如果采用非极性低分子量有机物为非极性有机膜层时,如蜡、分子量≤2000 的聚烯烃或聚苯乙烯以及石油树脂等, 非极性低分子量有机物一般在环境中都可生物 降解, 因此本发明环保复合包膜型缓释肥料仍然是完全环保型缓释肥料。 即使非极性 有机膜层材料采用非极性聚合物, 由于其使用量仅约 1%左右, 与现有技术中的缓释肥 料相比, 其对环境的污染是很小的, 具有明显优点。 The invention can be made in the coating of the environmentally friendly composite coated slow release fertilizer of the present invention by recombining a very thin high barrier organic film layer (the amount of which is small, which is smaller than the amount of the sulfur film layer which can be separately protected). The release period of the environmentally friendly composite coated slow release fertilizer is further prolonged, especially when the high barrier organic film layer is a non-polar organic film layer, and the non-polar organic film layer is closely attached to the sulfur film layer, the effect is obvious. Therefore, the release period of the environmentally friendly composite coated slow release fertilizer of the present invention in which the non-polar organic film layer is compounded in the envelope can be long. Moreover, a polar organic substance or other slow release modifier which is soluble in the high barrier organic film layer material is added to the high barrier organic film layer, and the release period can be freely adjusted by controlling the addition amount, and the coating film is changed more than the coating film. The method of adjusting the release period of the total thickness of the layer is more efficient and more economical. In particular, if a non-polar low molecular weight organic material is used as a non-polar organic film layer, such as wax, polyolefin or polystyrene having a molecular weight of ≤2000, and petroleum resin, non-polar low molecular weight organic substances are generally available in the environment. Biodegradable, therefore, the environmentally friendly composite coated slow release fertilizer of the present invention is still a completely environmentally friendly slow release fertilizer. Even if the non-polar organic film layer material uses a non-polar polymer, since it is used in an amount of only about 1%, it has little environmental pollution compared with the slow-release fertilizer of the prior art, and has obvious advantages. .
附图说明 DRAWINGS
图 1是本发明环保复合包膜型缓释肥料的球状肥料芯 1一含硫可降解聚合物混合 物膜层 3—硫磺膜层 2—含硫可降解聚合物混合物膜层 3结构图。 BRIEF DESCRIPTION OF THE DRAWINGS Fig. 1 is a structural view of a spherical fertilizer core 1 - a sulfur-containing degradable polymer mixture film - a sulfur film layer 2 - a sulfur-containing degradable polymer mixture film layer 3 of the environmentally friendly composite film type slow release fertilizer of the present invention.
图 2是本发明环保复合包膜型缓释肥料的球状肥料芯 1一硫磺膜层 2—含硫可降解 聚合物混合物膜层 3结构图。 Fig. 2 is a structural view of a spherical fertilizer core 1 - sulfur film layer 2 - sulfur-containing degradable polymer mixture film layer 3 of the environmentally friendly composite film type slow release fertilizer of the present invention.
图 3是本发明环保复合包膜型缓释肥料的球状肥料芯 1一可降解聚合物膜层 4一硫 磺膜层 2—可降解聚合物膜层 4结构图。 Fig. 3 is a structural view of a spherical fertilizer core 1 - a degradable polymer film layer 4 - a sulfur film layer 2 - a degradable polymer film layer 4 of the environmentally friendly composite film type slow release fertilizer of the present invention.
图 4是本发明环保复合包膜型缓释肥料的球状肥料芯 1一硫磺膜层 2—可降解聚合 物膜层 4结构图。 Fig. 4 is a structural view of a spherical fertilizer core 1 - sulfur film layer 2 - a degradable polymer film layer 4 of the environmentally friendly composite coated slow release fertilizer of the present invention.
图 5是本发明环保复合包膜型缓释肥料的球状肥料芯 1一含硫可降解聚合物混合 物膜层 3—硫磺膜层 2—可降解聚合物膜层 4结构图。 Fig. 5 is a structural view of a spherical fertilizer core 1 - sulfur-degradable polymer mixture film 3 - sulfur film layer 2 - degradable polymer film layer 4 of the environmentally friendly composite film type slow release fertilizer of the present invention.
图 6是本发明环保复合包膜型缓释肥料的球状肥料芯 1一可降解聚合物膜层 4一硫 磺膜层 2—含硫可降解聚合物混合物膜层 3结构图。 Figure 6 is a spherical fertilizer core 1 of the environmentally friendly composite coated slow release fertilizer of the present invention, a degradable polymer film layer 4 sulfur Sulfide layer 2 - structure diagram of film layer 3 of sulfur-containing degradable polymer mixture.
图 7是本发明环保复合包膜型缓释肥料的球状肥料芯 1一含硫可降解聚合物混合 物膜层 3—硫磺膜层 2—含硫可降解聚合物混合物膜层 3—可降解聚合物膜层 4结构图。 7 is a spherical fertilizer core 1 of a sulfur-containing degradable polymer mixture layer of the environmentally friendly composite coated slow release fertilizer of the present invention. 3 - a sulfur film layer 2 - a sulfur-containing degradable polymer mixture film layer 3 - a degradable polymer Structure of the film layer 4.
图 8是本发明环保复合包膜型缓释肥料的球状肥料芯 1一硫磺膜层 2—含硫可降解 聚合物混合物膜层 3—可降解聚合物膜层 4结构图。 Fig. 8 is a structural view of a spherical fertilizer core 1 - sulfur film layer 2 - sulfur-degradable polymer mixture film layer 3 - degradable polymer film layer 4 of the environmentally friendly composite film type slow release fertilizer of the present invention.
图 9是本发明环保复合包膜型缓释肥料的球状肥料芯 1一含硫可降解聚合物混合 物膜层 3—硫磺膜层 2—高阻透有机膜层 5—含硫可降解聚合物混合物膜层 3结构图。 9 is a spherical fertilizer core 1 of a sulfur-containing degradable polymer mixture layer 3 - a sulfur film layer 2 - a high barrier organic film layer 5 - a sulfur-containing degradable polymer mixture of the environmentally friendly composite coated slow release fertilizer of the present invention Structure of the film layer 3.
图 10是本发明环保复合包膜型缓释肥料的球状肥料芯 1一含硫可降解聚合物混合 物膜层 3—硫磺膜层 2—高阻透有机膜层 5—可降解聚合物膜层 4结构图。 Figure 10 is a spherical fertilizer core 1 of a sulfur-containing degradable polymer mixture of the environmentally friendly composite coated slow release fertilizer of the present invention. 3 - Sulfur film layer 2 - High barrier organic film layer 5 - Degradable polymer film layer 4 Structure diagram.
图 11是本发明环保复合包膜型缓释肥料的球状肥料芯 1一高阻透有机膜层 5—硫 磺膜层 2—含硫可降解聚合物混合物膜层 3结构图。 Figure 11 is a structural view of a spherical fertilizer core 1 - a high barrier organic film layer 5 - a sulfur film layer 2 - a sulfur-containing degradable polymer mixture film layer 3 of the environmentally friendly composite film type slow release fertilizer of the present invention.
图 12是本发明环保复合包膜型缓释肥料的球状肥料芯 1一高阻透有机膜层 5—硫 磺膜层 2—可降解聚合物膜层 4结构图。 Fig. 12 is a structural view of a spherical fertilizer core 1 - a high barrier organic film layer 5 - a sulfur film layer 2 - a degradable polymer film layer 4 of the environmentally friendly composite film type slow release fertilizer of the present invention.
具体实施方式 detailed description
本发明环保复合包膜型缓释肥料由肥料芯 1和肥料芯外面的包膜组成, 包膜包含 (a) 硫磺膜层 2, (b) 含硫可降解聚合物混合物膜层 3和 I或可降解聚合物膜层 4, 有或无 (c) 高阻透有机膜层 5; 其中, 硫磺膜层是整个包膜的里层或中间层。 The environmentally friendly composite coated slow release fertilizer of the present invention is composed of a fertilizer core 1 and a coating film outside the fertilizer core, and the coating film comprises (a) a sulfur film layer 2, (b) a sulfur-containing degradable polymer mixture film layer 3 and I or Degradable polymer film layer 4, with or without (c) high barrier organic film layer 5; wherein the sulfur film layer is the inner or intermediate layer of the entire envelope.
本发明环保复合包膜型缓释肥料的肥料芯, 可以是氮肥、 磷肥、 钾肥或复混肥等。 肥料芯的形状可以是粒状、 片状等, 但以粒状为佳, 最好是球状。 The fertilizer core of the environmentally friendly composite coated slow release fertilizer of the invention may be nitrogen fertilizer, phosphate fertilizer, potassium fertilizer or compound fertilizer. The shape of the fertilizer core may be granular, flake, or the like, but it is preferably granular, and preferably spherical.
本发明中的含硫可降解聚合物混合物膜层是指硫磺与可降解聚合物的混合物膜 层。 本发明环保复合包膜型缓释肥料的包膜可以是含硫可降解聚合物混合物膜层与硫 磺膜层的复合膜层, 这种复合膜层是优选。 此时, 缓释肥料的结构可以如附图 1 和附 图 2所示, 附图 1结构比附图 2结构优。 The film of the sulfur-containing degradable polymer mixture in the present invention means a film layer of a mixture of sulfur and a degradable polymer. The coating of the environmentally friendly composite coated slow release fertilizer of the present invention may be a composite film layer of a sulfur-containing degradable polymer mixture film layer and a sulfur film layer, and such a composite film layer is preferred. At this time, the structure of the slow release fertilizer can be as shown in Fig. 1 and Fig. 2, and the structure of Fig. 1 is superior to that of Fig. 2.
本发明环保复合包膜型缓释肥料的包膜也可以是可降解聚合物膜层与硫磺膜层的 复合膜层。 此时, 缓释肥料的结构可以如附图 3和附图 4所示, 附图 3结构比附图 4 结构优。 The envelope of the environmentally friendly composite coated slow release fertilizer of the present invention may also be a composite film layer of a degradable polymer film layer and a sulfur film layer. At this time, the structure of the slow-release fertilizer can be as shown in Fig. 3 and Fig. 4, and the structure of Fig. 3 is superior to that of Fig. 4.
本发明环保复合包膜型缓释肥料的包膜还可以是含硫可降解聚合物混合物膜层、 可 降解聚合物膜层和硫磺膜层三者的复合膜层。 其中, 含硫可降解聚合物混合物膜层紧贴 硫磺膜层的结构是优选, 并且含硫可降解聚合物混合物膜层紧贴硫磺膜层里表面的结构 比含硫可降解聚合物混合物膜层紧贴硫磺膜层外表面的结构优。 此时, 缓释肥料的结构 可以如附图 5、 附图 6、 附图 7和附图 8所示。 其中, 附图 5和附图 7是上述四种结构 中的优选, 附图 7结构比附图 5结构优。 此外, 还可以是其它组合方式的结构。 本发明环保复合包膜型缓释肥料的包膜可以在上述三大类结构的各结构中再复合 高阻透有机膜层。 高阻透有机膜层是指对水和肥料的透过率低于可降解聚合物膜层的 膜层, 即高阻透有机膜层材料对水和肥料的透过率低于包膜中所采用的可降解聚合物 对水和肥料的透过率。 由于非极性有机膜层对水和肥料的透过率很低, 水和肥料主要 从膜缺陷处透过, 因此本发明环保复合包膜型缓释肥料包膜中的高阻透有机膜层最好 为非极性有机膜层。 并且, 非极性有机膜层以紧贴硫磺膜层为优选, 非极性有机膜层 最好不是包膜的最外膜层。 The coating of the environmentally friendly composite coated slow release fertilizer of the present invention may also be a composite film layer of a sulfur-containing degradable polymer mixture film layer, a degradable polymer film layer and a sulfur film layer. Wherein, the structure of the sulfur-containing degradable polymer mixture film layer is close to the sulfur film layer, and the film layer of the sulfur-containing degradable polymer mixture is close to the surface of the sulfur film layer than the sulfur-containing degradable polymer mixture film layer. The structure close to the outer surface of the sulfur film layer is excellent. At this time, the structure of the slow release fertilizer can be as shown in Fig. 5, Fig. 6, Fig. 7, and Fig. 8. Among them, Fig. 5 and Fig. 7 are preferred among the above four structures, and the structure of Fig. 7 is superior to the structure of Fig. 5. In addition, it is also possible to have a structure of other combinations. The coating of the environmentally friendly composite coated slow release fertilizer of the present invention can further compound a high barrier organic film layer in each of the above three types of structures. The high barrier organic film layer refers to a film layer having a lower transmittance to water and fertilizer than the degradable polymer film layer, that is, the high barrier organic film layer material has a lower transmittance to water and fertilizer than in the envelope film. The permeability of water and fertilizer used by degradable polymers. Since the non-polar organic film layer has a low transmittance to water and fertilizer, water and fertilizer are mainly transmitted through the film defect, so the high-barrier organic film layer in the environmentally friendly composite coated slow release fertilizer coating of the present invention It is preferably a non-polar organic film layer. Further, the non-polar organic film layer is preferably adhered to the sulfur film layer, and the non-polar organic film layer is preferably not the outermost film layer of the envelope.
包膜中没有非极性有机膜层时, 含硫可降解聚合物混合物膜层紧贴硫磺膜层的结 构为优选结构。 但是, 包膜中有非极性有机膜层时, 非极性有机膜层紧贴硫磺膜层比 含硫可降解聚合物混合物膜层紧贴硫磺膜层更优先考虑, 非极性有机膜层紧贴硫磺膜 层的结构为更优选结构。在硫磺膜层的里表面和外表面可以都复合有非极性有机膜层。 因为非极性低分子量有机物的熔点低, 因此非极性低分子量有机膜层一般处于硫磺膜 层的外表面为好; 而非极性聚合物处于硫磺膜层的里表面和外表面都可以, 但一般仅 在一面存在即可以, 且以在里表面时发挥的阻透效果更佳。 在非极性有机膜层紧贴硫 磺膜层的结构中, 当在包膜中同时还有含硫可降解聚合物混合物膜层时, 含硫可降解 聚合物混合物膜层紧贴未贴有非极性有机膜层的硫磺膜层另一表面和 /或再紧贴于非 极性有机膜层表面的结构又是其中的更优化结构。 When there is no non-polar organic film layer in the envelope, the structure of the sulfur-containing degradable polymer mixture film layer adhering to the sulfur film layer is a preferred structure. However, when there is a non-polar organic film layer in the coating, the non-polar organic film layer is closely attached to the sulfur film layer, and the sulfur-containing degradable polymer mixture film layer is more closely adhered to the sulfur film layer, and the non-polar organic film layer is more preferred. The structure closely adjacent to the sulfur film layer is a more preferable structure. The inner surface and the outer surface of the sulfur film layer may be combined with a non-polar organic film layer. Since the non-polar low molecular weight organic substance has a low melting point, the non-polar low molecular weight organic film layer is generally on the outer surface of the sulfur film layer; the non-polar polymer is on the inner surface and the outer surface of the sulfur film layer, However, it is generally only available on one side, and the barrier effect exerted on the inner surface is better. In the structure in which the non-polar organic film layer is in close contact with the sulfur film layer, when there is a film layer of the sulfur-containing degradable polymer mixture in the coating film, the film layer of the sulfur-containing degradable polymer mixture is closely attached to the non-attached non-paste layer. The other surface of the sulfur film layer of the polar organic film layer and/or the structure which is in close contact with the surface of the non-polar organic film layer is a more optimized structure among them.
附图 9~附图 12所示的结构是复合有高阻透有机膜层的本发明环保复合包膜型缓 释肥料的四个代表结构。 还可以是其它组合方式的结构。 The structure shown in Fig. 9 to Fig. 12 is four representative structures of the environmentally friendly composite coated type slow release fertilizer of the present invention which is compounded with a high barrier organic film layer. It can also be a structure of other combinations.
当然, 还可以是在附图 1〜附图 12的结构基础上的变化结构。 比如, 可以是附图 1〜附图 12所示包膜结构的多重复合结构, 还可以是附图 1〜附图 12所示的包膜结构 之间相互组合的多重复合结构。但从工艺角度考虑, 这些多重复合结构不是优选结构。 Of course, it is also possible to change the structure based on the structures of Figs. 1 to 12. For example, it may be a multiple composite structure of the envelope structure shown in Figs. 1 to 12, or a multiple composite structure in which the envelope structures shown in Figs. 1 to 12 are combined with each other. However, these multiple composite structures are not preferred structures from a process perspective.
本发明环保复合包膜型缓释肥料的含硫可降解聚合物混合物膜层中, 硫磺的平均 质量分数可以在 0%~95%之间。 但是, 硫磺含量太低时, 膜层阻透性的提高效果不明 显,但太高时膜层的韧性低,呈脆性, 因此以在 20%~90%之间为佳,最好在 60%〜90% 之间。 必要时, 在含硫可降解聚合物混合物膜层中可以加入一定含量的增塑剂来提高 膜层的韧性。 同时, 还可以在含硫可降解聚合物混合物膜层中形成含硫梯度分布, 比 如硫磺膜层往外 (即与往肥料芯的方向相反) 的含硫可降解聚合物混合物膜层中含硫 量从里往外逐渐减小, 外层的含硫量低以使外层具有高的韧性。 当硫磺膜层往外的含 硫可降解聚合物混合物膜层中的含硫量高, 比如 80%以上时, 含硫可降解聚合物混合 物膜层外可以有一层薄(如 3~10 ί ΐη)的可降解聚合物膜层, 以更好地保护内部膜层。 In the film of the sulfur-containing degradable polymer mixture of the environmentally friendly composite coated slow-release fertilizer of the present invention, the average mass fraction of sulfur may be between 0% and 95%. However, when the sulfur content is too low, the effect of improving the barrier property of the film layer is not obvious, but when the content is too high, the toughness of the film layer is low and brittle, so it is preferably between 20% and 90%, preferably 60%. Between ~90%. If necessary, a certain amount of plasticizer may be added to the film layer of the sulfur-containing degradable polymer mixture to increase the toughness of the film. At the same time, it is also possible to form a sulfur-containing gradient distribution in the film layer of the sulfur-containing degradable polymer mixture, for example, the sulfur content in the film layer of the sulfur-containing degradable polymer mixture outside the sulfur film layer (ie, opposite to the direction toward the fertilizer core). Gradually decreasing from the inside to the outside, the outer layer has a low sulfur content to give the outer layer high toughness. When the sulfur content of the sulfur-containing degradable polymer mixture film layer outside the sulfur film layer is high, for example, 80% or more, the sulfur-containing degradable polymer mixture film layer may have a thin layer (such as 3~10 ί ΐη). A layer of degradable polymer film to better protect the inner film layer.
本发明环保复合包膜型缓释肥料采用的可降解聚合物, 可以是氨基树脂、 聚乙烯 醇及其共聚物的髙缩醛度缩醛树脂、 不饱和油树脂和天然聚合物及其衍生物等一种或 一种以上。 其中, 天然聚合物及其衍生物可以是硝酸纤维素、 紫胶、 醋酸纤维素、 交 联淀粉、 甲壳素衍生物和木质素衍生物等中的一种或一种以上。 本发明环保复合包膜 型缓释肥料包膜中的可降解聚合物是非水溶性的,或者尽管采用的预聚物是水溶性的, 但是最终形成的膜层中可降解聚合物应成为非水溶性的, 比如形成脲醛树脂和三聚氰 胺-甲醛树脂的预聚物可以是水溶性的, 但是经固化交联形成的脲醛树脂和三聚氰胺- 甲醛树脂成为了非水溶性的。 The biodegradable composite film type slow release fertilizer of the invention adopts a degradable polymer, which can be an amino resin or a polyethylene. One or more of a acetal acetal resin, an unsaturated oleoresin, a natural polymer, and a derivative thereof, of an alcohol and a copolymer thereof. Among them, the natural polymer and its derivative may be one or more of nitrocellulose, shellac, cellulose acetate, crosslinked starch, chitin derivative, and lignin derivative. The degradable polymer in the environmentally friendly composite coated slow release fertilizer coating of the present invention is water-insoluble, or although the prepolymer used is water-soluble, the degradable polymer in the finally formed film layer should be non-water soluble. The prepolymer such as a urea-formaldehyde resin and a melamine-formaldehyde resin may be water-soluble, but the urea-formaldehyde resin and the melamine-formaldehyde resin formed by curing cross-linking become water-insoluble.
在所述的可降解聚合物中, 氨基树脂是优选之一, 尤其是脲醛树脂和三聚氰胺-甲 醛树脂 (包括改性脲醛树脂和改性三聚氰胺 -甲醛树脂) 的价格低, 采用它们作为可降 解聚合物包膜材料制备的本发明环保复合包膜型缓释肥料是完全的以肥包肥型缓释肥 料, 肥分含量高, 产品成本较低; 特别是三聚氰胺-甲醛树脂对水和肥料的阻透性相对 较强, 并且其降解速度较慢, 其包膜可以在很长的时间期间中发挥包膜阻透作用。 其 次, 不饱和油树脂是不饱和油交联反应而成的树脂, 不饱和油包膜过程中可以不用溶 剂, 因此不饱和油树脂也可以是优选。 不饱和油是指分子结构中含有双键、 可以发生 交联反应的天然油, 比如桐油、 大豆油、 亚麻油或脱水蓖麻油等, 其中的桐油是价格 较低的天然不饱和油, 其交联形成的桐油树脂膜层对水和肥料的阻透性也较强, 是可 优选的不饱和油。 此外, 非水溶性的聚乙烯醇及其共聚物的髙缩醛度缩醛树脂 (縮醛 度 50%)和硝酸纤维素也是可考虑选用的可降解包膜材料。 聚乙烯醇及其共聚物的 缩醛树脂可以是聚乙烯醇及其共聚物的缩甲醛树脂、 缩乙醛树脂或缩丁醛树脂等。 Among the degradable polymers, amino resins are preferred, especially urea-formaldehyde resins and melamine-formaldehyde resins (including modified urea-formaldehyde resins and modified melamine-formaldehyde resins) at low prices, and they are used as degradable polymerization. The environmentally-friendly composite coated slow-release fertilizer prepared by the material of the coating material is a complete fertilizer-fermented slow-release fertilizer with high fertilizer content and low product cost; in particular, the resistance of melamine-formaldehyde resin to water and fertilizer The permeability is relatively strong, and its degradation rate is slow, and its envelope can exert an envelope barrier effect for a long period of time. Further, the unsaturated oleoresin is a resin obtained by crosslinking an unsaturated oil, and a solvent may not be used in the process of coating the unsaturated oil, so that an unsaturated oleoresin may also be preferred. Unsaturated oil refers to a natural oil that contains a double bond in the molecular structure and can undergo a cross-linking reaction, such as tung oil, soybean oil, linseed oil or dehydrated castor oil. Among them, tung oil is a lower-priced natural unsaturated oil. The tung oil resin film formed in combination has a strong barrier property against water and fertilizer, and is a preferred unsaturated oil. Further, the acetal acetal resin (50% acetal degree) and nitrocellulose of the water-insoluble polyvinyl alcohol and its copolymer are also degradable coating materials which are considered to be selected. The acetal resin of polyvinyl alcohol and its copolymer may be a formal resin, a acetal resin or a butyral resin of polyvinyl alcohol and a copolymer thereof.
为了调节含硫可降解聚合物混合物膜层和可降解聚合物膜层的性能, 比如韧性等, 在含硫可降解聚合物混合物膜层和可降解聚合物膜层中都可以加入低分子有机物比如 前述的增塑剂等, 还可以加入少量的杀菌剂或抑菌剂。 In order to adjust the properties of the sulfur-containing degradable polymer mixture film layer and the degradable polymer film layer, such as toughness, a low molecular organic substance such as a sulfur-containing degradable polymer mixture film layer and a degradable polymer film layer may be added. A small amount of a bactericide or a bacteriostatic agent may be added to the aforementioned plasticizer or the like.
为了进一步提高本发明环保复合包膜型缓释肥料的释放期, 包膜中最好复合有高 阻透有机膜层, 高阻透有机膜层材料可以是髙阻透性低分子有机物, 也可以是高阻透 性的难降解聚合物。 高阻透性低分子有机物可以是沥青及其混合物和松香(酯) 及其 混合物等低透过性有机物(相对于可降解聚合物而言), 高阻透性的难降解聚合物可以 是丙烯腈一丁二烯一苯乙烯共聚物(ABS)、 丁腈橡胶、 不饱和聚酯、 聚氨酯和环氧树 脂等低透过性聚合物(相对于可降解聚合物而言)。 高阻透有机膜层尤以非极性有机膜 层为优先选择, 并且非极性有机膜层最好紧贴硫磺膜层, 且最好不是包膜的最外膜层。 非极性有机膜层的材料可以是非极性低分子量有机物和 I或非极性聚合物, 其中非极 性有机膜层以仅采用非极性低分子量有机物为优选。 In order to further improve the release period of the environmentally friendly composite coated slow-release fertilizer of the present invention, it is preferable to compound a high-barrier organic film layer in the coating, and the high-barrier organic film layer material may be a ruthenium-blocking low-molecular organic substance or It is a highly barrier-resistant, refractory polymer. The high-barrier low-molecular organic substance may be a low-permeability organic substance (relative to a degradable polymer) such as pitch and a mixture thereof and rosin (ester) and a mixture thereof, and the high-barrier refractory polymer may be propylene. Low permeability polymer (relative to degradable polymers) such as nitrile-butadiene-styrene copolymer (ABS), nitrile rubber, unsaturated polyester, polyurethane and epoxy resin. The high-barrier organic film layer is preferably a non-polar organic film layer, and the non-polar organic film layer is preferably in close contact with the sulfur film layer, and is preferably not the outermost film layer of the envelope. The material of the non-polar organic film layer may be a non-polar low molecular weight organic substance and an I or a non-polar polymer, wherein the non-polar organic film layer is preferably a non-polar low molecular weight organic substance.
本发明环保复合包膜型缓释肥料中, 非极性有机膜层所采用的非极性低分子量有 机物可以是熔点≥40 的蜡、 熔点或软化点≥40°C且分子量≤2000 的低分子量聚烯烃或 聚苯乙烯以及软化点≥40Ό的石油树脂等中的一种或一种以上。其中,蜡可以是石油蜡、 合成蜡、 天然蜡、 矿物蜡等; 低分子量聚烯烃可以是聚乙烯蜡, 也可以是低分子量聚 丙烯、 低分子量聚异丁烯等其它低分子量聚烯烃。 当然, 低分子量聚烯烃或聚苯乙烯 的分子量也可以≥2000。 非极性低分子量有机物的熔点或软化点较高为好, 以≥60'。为 佳, 最好≥85°C。 In the environmentally friendly composite coated slow release fertilizer of the present invention, the nonpolar polar molecular layer used in the nonpolar organic film layer has The organic substance may be one or more of a wax having a melting point of ≥ 40, a melting point or a low molecular weight polyolefin or polystyrene having a melting point of ≥ 40 ° C and a molecular weight of ≤ 2000, and a petroleum resin having a softening point of ≥ 40 Å. The wax may be a petroleum wax, a synthetic wax, a natural wax, a mineral wax or the like; the low molecular weight polyolefin may be a polyethylene wax, or may be a low molecular weight polypropylene, a low molecular weight polyisobutylene or the like. Of course, the molecular weight of the low molecular weight polyolefin or polystyrene may also be ≥2000. The melting point or softening point of the non-polar low molecular weight organic substance is preferably higher, ≥ 60'. Preferably, it is preferably ≥85 °C.
本发明环保复合包膜型缓释肥料中, 可以釆用聚烯烃、 聚苯乙烯、 顺丁橡胶、 天 然橡胶、 聚异戊二烯橡胶、 丁苯橡胶、 丁基橡胶、 乙丙橡胶及三元乙丙橡胶、 苯乙烯 一丁二烯一苯乙烯嵌段共聚物和苯乙烯一异戊二烯一苯乙烯嵌段共聚物等一种或一种 以上的非极性聚合物作为非极性有机膜层材料。 In the environmentally friendly composite coated slow release fertilizer of the invention, polyolefin, polystyrene, butadiene rubber, natural rubber, polyisoprene rubber, styrene butadiene rubber, butyl rubber, ethylene propylene rubber and ternary can be used. One or more non-polar polymers such as ethylene propylene rubber, styrene-butadiene-styrene block copolymer and styrene-isoprene-styrene block copolymer as non-polar organic Film material.
可以在高阻透有机膜层中加入一定量的可溶于高阻透有机膜层材料的极性有机 物, 通过控制其加入量以自由地调节本发明环保复合包膜型缓释肥料的释放期。 比如, 在石蜡中加入带极性基团的蜡溶性添加剂如氯化石蜡、 松香及其酯、 沥青等; 在非极 性聚合物中加入极性增塑剂, 比如邻苯二甲酸二丁酯类、 多元醇酯类等。 极性有机物 可以是极性低分子量有机物(如上述举例), 也可以是极性预聚物或聚合物, 如石蜡中 加入不饱和聚酯预聚物, 包膜后使之交联。 当然, 在高阻透有机膜层中加入水溶性盐、 淀粉、 木粉、 植物屑、 粘土、 滑石粉、 分子筛粉或骨粉等其它可提高高阻透有机膜层 对水和肥料通透性的添加物, 也可以调节本发明环保复合包膜型缓释肥料的释放期。 A certain amount of polar organic substance soluble in the high-barrier organic film layer material may be added to the high-barrier organic film layer, and the release period of the environmentally-friendly composite coated type slow-release fertilizer of the present invention can be freely adjusted by controlling the amount of the organic substance added thereto. . For example, adding wax-soluble additives with polar groups such as chlorinated paraffins, rosins and their esters, asphalt, etc. to paraffin; adding polar plasticizers such as dibutyl phthalate to non-polar polymers Classes, polyol esters, etc. The polar organic substance may be a polar low molecular weight organic substance (as exemplified above), or may be a polar prepolymer or a polymer such as an unsaturated polyester prepolymer added to the paraffin wax, which is crosslinked by coating. Of course, the addition of water-soluble salts, starch, wood flour, plant chips, clay, talc, molecular sieve powder or bone powder to the high-barrier organic film layer can improve the permeability of the high-barrier organic film layer to water and fertilizer. The addition period can also adjust the release period of the environmentally friendly composite coated slow release fertilizer of the present invention.
肥料芯外面的包膜中硫磺膜层应是完整或基本完整的, 最好不要有大量的破损, 因此硫磺膜层应达到一定的平均厚度。硫磺膜层的平均厚度可以在 l~100/ m之间,但 以 8~60 m为优选。整个包膜的总平均厚度应能承担肥料芯吸水膨胀所产生的撑胀力, 而不致整体包膜被撑破, 因此包膜总平均厚度可以在 10~180 m之间。 根据硫磺膜层 8-60 m的优选平均厚度, 则包膜总平均厚度以 20~90 m为优选。 可降解聚合物膜 层和含硫可降解聚合物混合物膜层两者的总平均厚度可以为 5~180^ m,但以 8~50/ m 为优选。 高阻透有机膜层的总平均厚度可以为 0~15 m, 以 0~10/ m为优选。 硫磺膜 层往外的膜层平均厚度不应低于 3 m, 最好不低于 5 // m。 此外, 含硫可降解聚合物 混合物膜层的总平均厚度和可降解聚合物膜层的总平均厚度分别都可以为 0 100 / m, 但含硫可降解聚合物混合物膜层的总平均厚度以 8~50 m为优选, 可降解聚合物膜层 的总平均厚度以 0~35 m优选。 The sulfur film layer on the outer surface of the fertilizer core should be complete or substantially intact, and it is best not to have a large amount of damage, so the sulfur film layer should reach a certain average thickness. The average thickness of the sulfur film layer may be between l and 100/m, but it is preferably from 8 to 60 m. The total average thickness of the entire envelope should be able to bear the expansion force generated by the water swell of the fertilizer core, so that the overall envelope is broken, so the total average thickness of the envelope can be between 10 and 180 m. The total average thickness of the coating is preferably from 20 to 90 m, depending on the preferred average thickness of the sulfur film layer of from 8 to 60 m. The total average thickness of both the degradable polymer film layer and the sulfur-containing degradable polymer mixture film layer may be 5 to 180 m, but is preferably 8 to 50 m. The total average thickness of the high-barrier organic film layer may be 0 to 15 m, preferably 0 to 10/m. The average thickness of the outer layer of the sulfur film layer should not be less than 3 m, preferably not less than 5 // m. Further, the total average thickness of the film layer of the sulfur-containing degradable polymer mixture and the total average thickness of the degradable polymer film layer may each be 0 100 / m, but the total average thickness of the film layer of the sulfur-containing degradable polymer mixture is 8~50 m is preferred, and the total average thickness of the degradable polymer film layer is preferably 0 to 35 m.
当然, 包膜总平均厚度、 硫磺膜层平均厚度、 可降解聚合物膜层和含硫可降解聚 合物混合物膜层两者的总平均厚度、 含硫可降解聚合物混合物膜层的总平均厚度、 可 降解聚合物膜层的总平均厚度以及高阻透有机膜层的总平均厚度等都可以比上述提出 的各自高限值更大。 这些厚度愈大, 则环保复合包膜型缓释肥料的释放期会愈长。 由于硫磺、 可降解聚合物和高阻透有机膜层材料之间的表面性质不同, 为了调节 它们之间相互润湿铺展成膜性, 可以在可降解聚合物、 含硫可降解聚合物和髙阻透有 机膜层材料包膜液中加入表面活性剂。 Of course, the total average thickness of the envelope, the average thickness of the sulfur film layer, the total average thickness of both the degradable polymer film layer and the sulfur-containing degradable polymer mixture film layer, and the total average thickness of the sulfur-containing degradable polymer mixture film layer The total average thickness of the degradable polymer film layer and the total average thickness of the high-barrier organic film layer can be compared with the above The respective upper limit values are larger. The greater these thicknesses, the longer the release period of the environmentally friendly composite coated slow release fertilizer. Due to the different surface properties between the sulfur, the degradable polymer and the high barrier organic film layer material, in order to adjust the mutual wetting and spreading film formation between them, the degradable polymer, the sulfur-containing degradable polymer and the ruthenium may be used. A surfactant is added to the coating liquid of the organic film layer.
此外, 本发明环保复合包膜型缓释肥料包膜中的硫磺膜层、 含硫可降解聚合物混 合物膜层、 可降解聚合物膜层和髙阻透有机膜层中都可以添加各种其它添加物, 以达 到诸如进一步调节各膜层的某种性能或降低成本等的目的。 In addition, various other additives may be added to the sulfur film layer, the sulfur-containing degradable polymer mixture film layer, the degradable polymer film layer and the antimony-barrier organic film layer in the environmentally-friendly composite coated slow release fertilizer coating of the present invention. The additive is added for purposes such as further adjusting a certain property of each film layer or reducing cost.
下面以尿素作为肥料芯的本发明环保复合包膜型缓释尿素为例, 说明本发明环保 复合包膜型缓释肥料的具体实施方法和发明效果。 采用水中溶出法评价本发明环保复 合包膜型缓释尿素的缓释性能, 水中溶出法是测定本发明环保复合包膜型缓释尿素中 尿素在水中的溶出速率, 具体做法是: 将 10克本发明环保复合包膜型缓释尿素浸泡于 200毫升的水中, 25°C恒温浸泡,测定初期溶出率和平均微分溶出率。初期溶出率 ^是 指最初开始浸泡的 24h内溶出的尿素质量占所取 10克本发明环保复合包膜型缓释尿素 中尿素总质量的百分数,而平均微分溶出率¾^则是从浸泡第 2天到第 7天每天平均溶 出的尿素质量占所取 10克本发明环保复合包膜型缓释尿素中尿素总质量的百分数。根 据初期溶出率 ^和平均微分溶出率 ^,,计算本发明环保复合包膜型缓释尿素在水中的 释放期 t (天): Hereinafter, the environmentally friendly composite coated slow release urea of the present invention using urea as a fertilizer core is taken as an example to illustrate the specific implementation method and invention effect of the environmentally friendly composite coated slow release fertilizer of the present invention. The slow release property of the environmentally friendly composite coated slow release urea of the present invention is evaluated by the dissolution method in water. The dissolution method in water is the determination of the dissolution rate of urea in water in the environmentally friendly composite coated slow release urea of the present invention, and the specific method is as follows: 10 g The environmentally friendly composite coated slow release urea of the invention is immersed in 200 ml of water and immersed at a constant temperature of 25 ° C to measure the initial dissolution rate and the average differential dissolution rate. The initial dissolution rate ^ refers to the percentage of urea dissolved in the first 24 hours of immersion in the total mass of urea in the environmentally friendly composite coated slow release urea of the invention, and the average differential dissolution rate is 3⁄4^ from the soaking The average amount of urea dissolved per day from 2 days to 7 days is 10% of the total mass of urea in the environmentally-friendly composite coated slow-release urea of the present invention. According to the initial dissolution rate ^ and the average differential dissolution rate ^, the release period of the environmentally friendly composite coated slow release urea of the present invention in water is calculated (day):
Ψ Ψ
实施例 1 Example 1
将粒径为 2.0~4.0mm的粒状工业尿素加入流化床包膜设备中, 并使粒状尿素处于 沸腾状态, 流化床中粒状尿素温度保持在 80°C。 将脲醛树脂预聚物水溶液(脲醛树脂 预聚物是尿素:甲醛摩尔比为 1: 2的尿素与甲醛反应所制备)和 150°C左右的熔融硫 磺分别从两组不同的喷嘴同时往粒状尿素表面慢慢喷涂,通过控制它们的喷涂流量比, 使形成的含硫脲醛树脂混合物膜层中硫磺的平均质量分数为 70%, 喷涂直到形成的该 层含硫脲醛树脂混合物膜层质量达到最终成品环保复合包膜型缓释尿素总质量的 6%, 干燥除去膜层中含水。然后,停止喷涂脲醛树脂预聚物水溶液, 继续慢慢喷涂 15 TC左 右的熔融硫磺于含硫脲醛树脂混合物膜层表面, 直到形成的硫磺膜层质量达到最终成 品环保复合包膜型缓释尿素总质量的 7%。然后, 再在硫磺膜层表面喷涂含硫磺的脲醛 树脂预聚物水溶液(脲醛树脂预聚物是尿素:甲醛摩尔比为 1: 1.6的尿素与甲醛反应 所制备,硫磺:脲醛树脂预聚物之质量比为 2 : 3 ),直到形成的该层含硫脲醛树脂混合 物膜层质量达到最终成品环保复合包膜型缓释尿素总质量的 6%。 干燥除去膜层中含 水, 并使膜层中的脲醛树脂固化充分, 即得环保复合包膜型缓释尿素。 所制得的环保 复合包膜型缓释尿素的释放期为 145天。 The granular industrial urea having a particle diameter of 2.0 to 4.0 mm is introduced into the fluidized bed coating device, and the granular urea is in a boiling state, and the temperature of the granular urea in the fluidized bed is maintained at 80 °C. The urea-formaldehyde resin prepolymer aqueous solution (urea resin prepolymer is urea: formaldehyde is prepared by reacting urea with formaldehyde in a molar ratio of 1:2) and molten sulfur at about 150 °C from two different nozzles simultaneously to granular urea. The surface is slowly sprayed, and by controlling the spray flow ratio thereof, the average mass fraction of sulfur in the formed sulfur-containing urea-formaldehyde resin mixture layer is 70%, and spraying until the formed layer of the sulfur-containing urea-formaldehyde resin mixture reaches the final product quality. 6% of the total mass of the environmentally-friendly composite coated slow-release urea, drying to remove water in the film. Then, stop spraying the urea-formaldehyde resin prepolymer aqueous solution, and continue to spray about 15 TC of molten sulfur on the surface of the sulfur-containing urea-formaldehyde resin mixture film layer until the quality of the formed sulfur film layer reaches the final product environmentally friendly composite coated type slow-release urea total. 7% of the quality. Then, a sulfur-containing urea-formaldehyde resin prepolymer aqueous solution is sprayed on the surface of the sulfur film layer. The urea-formaldehyde resin prepolymer is prepared by reacting urea with formaldehyde in a molar ratio of 1:1.6, and sulfur: urea-formaldehyde resin prepolymer. The mass ratio is 2:3) until the film quality of the layer containing the thiourea resin mixture is 6% of the total mass of the final product environmentally friendly composite coated slow release urea. Drying removes the film layer Water, and the urea-formaldehyde resin in the film layer is fully cured, that is, an environmentally friendly composite coated type slow-release urea is obtained. The release period of the prepared environmentally-friendly composite coated slow release urea was 145 days.
实施例 2 Example 2
将粒径为 2.0~4.0mm的粒状工业尿素加入流化床包膜设备中, 并使粒状尿素处于 沸腾状态, 流化床中粒状尿素温度保持在 90°C。 将 150Ό左右熔融硫磺慢慢喷涂于尿 素表面,直到硫磺膜层质量达到最终成品环保复合包膜型缓释尿素总质量的 7%。然后, 在硫磺膜层表面再喷涂含硫磺的三聚氰胺一甲醛树脂预聚物水溶液(三聚氰胺一甲醛 树脂预聚物是三聚氰胺:甲酸摩尔比为 1: 3的三聚氰胺与甲醛反应所制备,硫磺:三 聚氰胺一甲醛树脂预聚物之质量比为 7: 3 ),直到形成的含硫三聚氰胺一甲醛树脂混合 物膜层质量达到最终成品环保复合包膜型缓释尿素总质量的 8%。 干燥除去膜层中含 水, 并使膜层中的三聚氰胺一甲醛树脂固化充分, 即得环保复合包膜型缓释尿素。 所 制得的环保复合包膜型缓释尿素的释放期为 112天。 The granular industrial urea having a particle diameter of 2.0 to 4.0 mm is introduced into the fluidized bed coating device, and the granular urea is in a boiling state, and the temperature of the granular urea in the fluidized bed is maintained at 90 °C. About 150 熔融 of molten sulfur is slowly sprayed on the surface of the urea until the quality of the sulfur film reaches 7% of the total mass of the final product environmentally friendly composite coated slow release urea. Then, a sulphur-containing melamine-formaldehyde resin prepolymer aqueous solution is sprayed on the surface of the sulfur film layer (melamine-formaldehyde resin prepolymer is prepared by reacting melamine with a molar ratio of 1:3 melamine and formaldehyde, sulfur: melamine one The mass ratio of the formaldehyde resin prepolymer is 7:3) until the film quality of the formed sulfur-containing melamine-formaldehyde resin mixture reaches 8% of the total mass of the final product environmentally friendly composite coated slow release urea. The water in the film layer is removed by drying, and the melamine-formaldehyde resin in the film layer is sufficiently cured to obtain an environmentally friendly composite coated type slow-release urea. The release period of the environmentally friendly composite coated slow release urea was 112 days.
实施例 3 Example 3
将粒径为 2.0~4.0mm的粒状工业尿素加入流化床包膜设备中, 并使粒状尿素处于 沸腾状态, 流化床中粒状尿素温度保持在 90°C。 将三聚氰胺一甲醛树脂预聚物水溶液 (三聚氰胺一甲醛树脂预聚物是三聚氰胺:甲醛摩尔比为 1: 4的三聚氰胺与甲醛反应 所制备) 喷涂于尿素表面, 直到形成的该层三聚氰胺一甲醛树脂膜层质量达到最终成 品环保复合包膜型缓释尿素总质量的 2%, 干燥除去膜层中含水。然后, 在三聚氰胺一 甲醛树脂膜层表面慢慢喷涂 150°C左右的熔融硫磺,直到形成的硫磺膜层质量达到最终 成品环保复合包膜型缓释尿素总质量的 11%。 最后, 再在硫磺膜层表面喷涂三聚氰胺 一甲酸树脂预聚物水溶液 (三聚氰胺一甲酸树脂预聚物是三聚氰胺:甲醛摩尔比为 1: 3的三聚氰胺与甲醛反应所制备), 直到形成的该层三聚氰胺一甲醛树脂膜层质量达到 最终成品环保复合包膜型缓释尿素总质量的 4%。干燥除去膜层中含水, 并使膜层中的 三聚氰胺一甲醛树脂固化充分, 即得环保复合包膜型缓释尿素。 所制得的环保复合包 膜型缓释尿素的释放期为 115天。 The granular industrial urea having a particle diameter of 2.0 to 4.0 mm is introduced into the fluidized bed coating device, and the granular urea is in a boiling state, and the temperature of the granular urea in the fluidized bed is maintained at 90 °C. Spraying a melamine-formaldehyde resin prepolymer aqueous solution (melamine-formaldehyde resin prepolymer is prepared by reacting melamine:melamine with a formaldehyde molar ratio of 1:4) onto formaldehyde, until the layer of melamine-formaldehyde resin film is formed. The layer quality reaches 2% of the total mass of the final finished environmentally friendly composite coated slow release urea, and the water is removed by drying. Then, molten sulphur of about 150 ° C is sprayed on the surface of the melamine-formaldehyde resin film layer until the quality of the formed sulfur film layer reaches 11% of the total mass of the final product environmentally friendly composite coated slow release urea. Finally, a melamine-formic acid resin prepolymer aqueous solution is sprayed on the surface of the sulfur film layer (the melamine-formic acid resin prepolymer is prepared by reacting melamine with a formaldehyde molar ratio of 1:3 and melamine) until the layer of melamine is formed. The quality of a formaldehyde resin film layer reaches 4% of the total quality of the final product environmentally friendly composite coated slow release urea. The water is removed from the film layer by drying, and the melamine-formaldehyde resin in the film layer is sufficiently cured to obtain an environmentally-friendly composite film-type slow-release urea. The release period of the environmentally-friendly composite membrane-type slow-release urea produced was 115 days.
实施例 4 Example 4
将粒径为 2.0〜4.0nm的粒状工业尿素加入流化床包膜设备中, 并使粒状尿素处于 沸腾状态, 流化床中粒状尿素温度保持在 9(TC。 将 150°C左右熔融硫磺慢慢喷涂于尿 素表面, 直到形成的硫磺膜层质量达到最终成品环保复合包膜型缓释尿素总质量的 16%。 然后, 再在硫磺膜层表面喷涂三聚氰胺一甲醛树脂预聚物水溶液(三聚氰胺一 甲醛树脂预聚物是三聚氰胺:甲醛摩尔比为 1: 2.7的三聚氰胺与甲醛反应所制备),直 到形成的三聚氰胺一甲醛树脂膜层质量达到最终成品环保复合包膜型缓释尿素总质量 的 4%。干燥除去膜层中含水, 并使膜层中的三聚氰胺一甲酸树脂固化充分, 即得环保 复合包膜型缓释尿素。 所制得的环保复合包膜型缓释尿素的释放期为 117天。 The granular industrial urea with a particle size of 2.0~4.0nm is added to the fluidized bed coating equipment, and the granular urea is in a boiling state. The temperature of the granular urea in the fluidized bed is maintained at 9 (TC. The molten sulfur is about 150 ° C slow. Slowly spray on the urea surface until the quality of the formed sulfur film reaches 16% of the total mass of the final product environmentally friendly composite coated slow release urea. Then, spray the melamine-formaldehyde resin prepolymer aqueous solution on the surface of the sulfur film (melamine one). The formaldehyde resin prepolymer is prepared by reacting melamine with a formaldehyde molar ratio of 1:2.7 in melamine and formaldehyde, until the quality of the formed melamine-formaldehyde resin film reaches the final quality of the final product environmentally friendly composite coated slow release urea. 4%. The water is removed from the film layer by drying, and the melamine-carboxylic acid resin in the film layer is sufficiently cured to obtain an environmentally-friendly composite film-type slow-release urea. The release period of the environmentally friendly composite coated slow release urea was 117 days.
实施例 5 Example 5
将粒径为 2.0~4.0mm的粒状工业尿素加入流化床包膜设备中, 并使粒状尿素处于 沸腾状态, 流化床中粒状尿素温度保持在 50°C。 将硝酸纤维素溶液(溶剂为乙醇、 丙 酮和乙酸戊酯三者的混合溶剂)和 150°C左右的熔融硫磺分别从两组不同的喷嘴同时往 粒状尿素表面慢慢喷涂, 通过控制它们的喷涂流量比, 使形成的含硫硝酸纤维素混合 物膜层中硫磺的平均质量分数为 80%, 喷涂直到形成的该层含硫硝酸纤维素混合物膜 层质量达到最终成品环保复合包膜型缓释尿素总质量的 6%, 干燥除去膜层中溶剂。然 后,停止喷涂硝酸纤维素溶液,继续慢慢喷涂 150°C熔融硫磺于含硫硝酸纤维素混合物 膜层表面, 直到形成的硫磺膜层质量达到最终成品环保复合包膜型缓释尿素总质量的 8%。 最后, 再在硫磺膜层表面喷涂硝酸纤维素溶液, 直到形成的硝酸纤维素膜层质量 达到最终成品环保复合包膜型缓释尿素总质量的 2%。充分干燥除去膜层中溶剂, 即得 环保复合包膜型缓释尿素。 所制得的环保复合包膜型缓释尿素的释放期为 134天。 The granular industrial urea having a particle diameter of 2.0 to 4.0 mm is introduced into the fluidized bed coating device, and the granular urea is in a boiling state, and the temperature of the granular urea in the fluidized bed is maintained at 50 °C. The nitrocellulose solution (the solvent is a mixed solvent of ethanol, acetone and amyl acetate) and the molten sulfur at about 150 °C are simultaneously sprayed from the two different nozzles to the surface of the granular urea, respectively, by controlling their spraying. The flow ratio is such that the average mass fraction of sulfur in the formed sulfur-containing nitrocellulose mixture film layer is 80%, and the film quality of the layer of sulfur-containing nitrocellulose mixture formed until the final layer of the environmentally friendly composite coated type slow-release urea is reached. 6% of the total mass, dry to remove the solvent in the film. Then, stop spraying the nitrocellulose solution, and continue to spray 150 ° C molten sulfur on the surface of the sulfur-containing nitrocellulose mixture membrane layer until the quality of the formed sulfur film layer reaches the total quality of the final product environmentally friendly composite coated slow release urea. 8%. Finally, the nitrocellulose solution is sprayed on the surface of the sulfur film layer until the quality of the formed nitrocellulose film reaches 2% of the total mass of the final product environmentally friendly composite coated slow release urea. The solvent in the film layer is sufficiently dried to obtain an environmentally friendly composite coated type slow-release urea. The release period of the environmentally friendly composite coated slow release urea was 134 days.
实施例 6 Example 6
将粒径为 2.0~4.0mm的粒状工业尿素加入流化床包膜设备中, 并使粒状尿素处于 沸腾状态, 流化床中粒状尿素温度保持在 80°C。 将三聚氰胺一甲醛树脂预聚物水溶液 (三聚氰胺一甲醛树脂预聚物是三聚氰胺:甲醛摩尔比为 1: 3.5的三聚氰胺与甲醛反 应所制备) 喷涂于尿素表面, 直到形成的三聚氰胺一甲醛树脂膜层质量达到最终成品 环保复合包膜型缓释尿素总质量的 1.5%, 干燥除去膜层中含水。 然后, 在三聚氰胺一 甲醛树脂膜层表面慢慢喷涂 150Ό左右熔融硫磺,直到形成的硫磺膜层质量达到最终成 品环保复合包膜型缓释尿素总质量的 8%。最后, 再将三聚氰胺一甲醛树脂预聚物水溶 液(三聚氰胺一甲醛树脂预聚物是三聚氰胺:甲醛摩尔比为 1: 3的三聚氰胺与甲醛反 应所制备)和 150Ό左右的熔融硫磺分别从两组不同的喷嘴同时慢慢往硫磺膜层表面喷 涂, 通过控制它们的喷涂流量比, 使形成的含硫三聚氰胺一甲醛树脂混合物膜层中硫 磺的平均质量分数为 80%, 直到形成的该层含硫三聚氰胺一甲醛树脂混合物膜层质量 达到最终成品环保复合包膜型缓释尿素总质量的 7%。干燥除去膜层中含水, 并使膜层 中的三聚氰胺一甲醛树脂固化充分, 即得环保复合包膜型缓释尿素。 所制得的环保复 合包膜型缓释尿素的释放期为 118天。 The granular industrial urea having a particle diameter of 2.0 to 4.0 mm is introduced into the fluidized bed coating device, and the granular urea is in a boiling state, and the temperature of the granular urea in the fluidized bed is maintained at 80 °C. Spraying a melamine-formaldehyde resin prepolymer aqueous solution (melamine-formaldehyde resin prepolymer is prepared by reacting melamine:melamine with a formaldehyde molar ratio of 1:3.5) with formaldehyde until the surface of the melamine-formaldehyde resin film is formed. The final product is 1.5% of the total mass of the environmentally-friendly composite coated slow-release urea, and the water is removed by drying. Then, about 150 熔融 of molten sulfur is sprayed on the surface of the melamine-formaldehyde resin film layer until the quality of the formed sulfur film layer reaches 8% of the total mass of the final product environmentally friendly composite coated slow release urea. Finally, a melamine-formaldehyde resin prepolymer aqueous solution (melamine-formaldehyde resin prepolymer is prepared by reacting melamine:melamine with a molar ratio of 1:3 and formaldehyde) and 150 Å of molten sulfur are respectively different from two groups. The nozzles are simultaneously sprayed onto the surface of the sulfur film layer, and by controlling the spray flow ratio thereof, the average mass fraction of sulfur in the formed sulfur-containing melamine-formaldehyde resin mixture layer is 80% until the formed layer of sulfur-containing melamine is formed. The film quality of the formaldehyde resin mixture reaches 7% of the total mass of the final product environmentally friendly composite coated slow release urea. The water is removed from the film layer by drying, and the melamine-formaldehyde resin in the film layer is sufficiently cured to obtain an environmentally-friendly composite film-type slow-release urea. The release period of the environmentally-friendly composite coated slow release urea was 118 days.
实施例 7 Example 7
将粒径为 2.0~4.0mm的粒状工业尿素加入流化床包膜设备中, 并使粒状尿素处于 沸腾状态, 流化床中粒状尿素温度保持在 90°C。 将含硫磺的三聚氰胺一甲醛树脂预聚 物水溶液(三聚氰胺一甲醛树脂预聚物是三聚氰胺:甲醛摩尔比为 1: 3的三聚氰胺与 甲醛反应所制备, 硫磺:三聚氰胺一甲醛树脂预聚物之质量比为 4 : 1 ) 喷涂于尿素表 面, 直到形成的该层含硫三聚氰胺一甲醛树脂混合物膜层质量达到最终成品环保复合 包膜型缓释尿素总质量的 5%, 干燥除去膜层中含水。 随后, 在含硫三聚氰胺一甲酸树' 脂混合物膜层表面慢慢喷涂 150Ό左右熔融硫磺,直到形成的硫磺膜层质量达到最终成 品环保复合包膜型缓释尿素总质量的 6%。然后, 再在硫磺膜层表面喷涂含硫磺的三聚 氰胺一甲醛树脂预聚物水溶液 (三聚氰胺一甲醛树脂预聚物是三聚氰胺:甲醛摩尔比 为 1: 3的三聚氰胺与甲醛反应所制备,硫磺:三聚氰胺一甲醒树脂预聚物之质量比为 7: 3),直到形成的该层含硫三聚氰胺一甲醛树脂混合物膜层质量达到最终成品环保复 合包膜型缓释尿素总质量的 3%。最后, 再在含硫三聚氰胺一甲醛树脂混合物膜层表面 喷涂三聚氰胺一甲醛树脂预聚物水溶液 (三聚氰胺一甲醛树脂预聚物是三聚氰胺:甲 醛摩尔比为 1: 1 的三聚氰胺与甲醛反应所制备), 直到形成的该层三聚氰胺一甲醛树 脂膜层质量达到最终成品环保复合包膜型缓释尿素总质量的 1%。 干燥除去膜层中含 水, 并使膜层中的三聚氰胺一甲醛树脂固化充分, 即得环保复合包膜型缓释尿素。 所 制得的环保复合包膜型缓释尿素的释放期为 146天。 The granular industrial urea having a particle diameter of 2.0 to 4.0 mm is introduced into the fluidized bed coating device, and the granular urea is in a boiling state, and the temperature of the granular urea in the fluidized bed is maintained at 90 °C. Preconcentration of sulphur-containing melamine-formaldehyde resin Aqueous solution (melamine-formaldehyde resin prepolymer is prepared by reacting melamine: melamine with a formaldehyde molar ratio of 1:3 and formaldehyde, sulfur: melamine-formaldehyde resin prepolymer has a mass ratio of 4:1) sprayed on the urea surface, Until the formed layer of the sulfur-containing melamine-formaldehyde resin mixture has a film quality of 5% of the total mass of the final product environmentally friendly composite coated slow release urea, the water is removed by drying. Subsequently, about 150 熔融 of molten sulfur is sprayed on the surface of the sulfur-containing melamine-formic acid tree's lipid mixture film layer until the quality of the formed sulfur film layer reaches 6% of the total mass of the final product environmentally friendly composite coated slow release urea. Then, a sulphur-containing melamine-formaldehyde resin prepolymer aqueous solution is sprayed on the surface of the sulfur film layer (melamine-formaldehyde resin prepolymer is prepared by reacting melamine with formaldehyde in a molar ratio of 1:3, and melamine: melamine The mass ratio of the waking resin prepolymer is 7:3) until the film quality of the layer of the sulfur-containing melamine-formaldehyde resin mixture formed reaches 3% of the total mass of the final product environmentally friendly composite coated slow release urea. Finally, a melamine-formaldehyde resin prepolymer aqueous solution is sprayed on the surface of the sulfur-containing melamine-formaldehyde resin mixture film layer (melamine-formaldehyde resin prepolymer is prepared by reacting melamine with a molar ratio of melamine of formaldehyde: 1:1). Until the formation of the layer of melamine-formaldehyde resin film layer quality reached 1% of the total quality of the final product environmentally friendly composite coated slow release urea. The water is removed from the film layer by drying, and the melamine-formaldehyde resin in the film layer is sufficiently cured to obtain an environmentally friendly composite coated type slow-release urea. The release period of the prepared environmentally-friendly composite coated slow release urea was 146 days.
实施例 8 Example 8
将粒径为 2.0~4.0mm的粒状工业尿素加入流化床包膜设备中, 并使粒状尿素处于 沸腾状态, 流化床中粒状尿素温度保持在 90°C。 将 150°C左右熔融硫磺慢慢喷涂于尿 素表面, 直到形成的硫磺膜层质量达到最终成品环保复合包膜型缓释尿素总质量的 9%。 然后, 在硫磺膜层表面喷涂含硫磺的脲醛树脂预聚物水溶液(脲醛树脂预聚物是 尿素:甲醛摩尔比为 1: 1.3的尿素与甲醛反应所制备, 硫磺:脲醛树脂预聚物之质量 比为 7: 3 ),直到形成的含硫脲醛树脂混合物膜层质量达到最终成品环保复合包膜型缓 释尿素总质量的 5%。最后, 再在含硫脲醛树脂混合物膜层表面喷涂脲醛树脂预聚物水 溶液(脲醛树脂预聚物是尿素:甲醛摩尔比为 1: 1.8的尿素与甲醛反应所制备),直到 形成的脲醛树脂膜层质量达到最终成品环保复合包膜型缓释尿素总质量的 1.5%。 干燥 除去膜层中含水, 并使膜层中的脲醛树脂固化充分, 即得环保复合包膜型缓释尿素。 所制得的环保复合包膜型缓释尿素的释放期为 105天。 The granular industrial urea having a particle diameter of 2.0 to 4.0 mm is introduced into the fluidized bed coating device, and the granular urea is in a boiling state, and the temperature of the granular urea in the fluidized bed is maintained at 90 °C. The molten sulfur at about 150 °C is slowly sprayed on the surface of the urea until the quality of the formed sulfur film reaches 9% of the total mass of the final product environmentally friendly composite coated slow release urea. Then, a sulfur-containing urea-formaldehyde resin prepolymer aqueous solution is sprayed on the surface of the sulfur film layer. The urea-formaldehyde resin prepolymer is prepared by reacting urea with formaldehyde in a molar ratio of 1:1.3, and sulfur: the quality of the urea-formaldehyde resin prepolymer. The ratio is 7:3) until the film quality of the formed sulfur-containing urea-formaldehyde resin mixture reaches 5% of the total mass of the final product environmentally friendly composite coated slow release urea. Finally, a urea-formaldehyde resin prepolymer aqueous solution is sprayed on the surface of the thiourea-containing resin mixture film layer (the urea-formaldehyde resin prepolymer is prepared by reacting urea with formaldehyde in a molar ratio of 1:1.8) until the urea-formaldehyde resin film is formed. The layer quality reaches 1.5% of the total quality of the finished product environmentally friendly composite coated slow release urea. Drying removes the water in the film layer and cures the urea-formaldehyde resin in the film layer sufficiently, that is, the environmentally friendly composite film-type slow-release urea is obtained. The release period of the environmentally friendly composite coated slow release urea was 105 days.
实施例 9 Example 9
将粒径为 2.0~4.0mm的粒状工业尿素加入流化床包膜设备中, 并使粒状尿素处于 沸腾状态, 流化床中粒状尿素温度保持在 70°C。 将桐油和 150Ό左右的熔融硫磺分别 从不同的喷嘴同时往粒状尿素表面慢慢喷涂, 通过控制它们的喷涂流量比, 使形成的 含硫桐油树脂混合物膜层中硫磺的平均质量分数为 70%, 喷涂直到形成的该层含硫桐 油树脂混合物膜层质量达到最终成品环保复合包膜型缓释尿素总质量的 5%。然后, 停 止喷涂桐油,继续慢慢喷涂 150Ό左右熔融硫磺在含硫桐油树脂混合物膜层表面,直到 形成的硫磺膜层质量达到最终成品环保复合包膜型缓释尿素总质量的 8%。然后, 再在 硫磺膜层表面喷涂分子量为 1500的聚乙烯蜡的苯溶液,直到形成的聚乙烯蜡膜层质量 达到最终成品环保复合包膜型缓释尿素总质量的 1.5%, 充分干燥除去苯。 最后, 再在 聚乙烯蜡膜层表面慢慢喷涂含硫磺的桐油 (含有桐油质量 0.4%的催干剂, 硫磺:桐油 之质量比为 1: 1 ),直到形成的含硫桐油树脂混合物膜层质量达到最终成品环保复合包 膜型缓释尿素总质量的 4%。使膜层中的桐油树脂固化充分, 即得环保复合包膜型缓释 尿素。 所制得的环保复合包膜型缓释尿素的释放期为 203天。 The granular industrial urea having a particle diameter of 2.0 to 4.0 mm is introduced into the fluidized bed coating device, and the granular urea is in a boiling state, and the temperature of the granular urea in the fluidized bed is maintained at 70 °C. Tung oil and about 150 熔融 of molten sulfur were sprayed from different nozzles simultaneously to the surface of granular urea. By controlling their spray flow ratio, the average mass fraction of sulfur in the formed sulfur-containing tung oil resin mixture film layer was 70%. Spraying until the formation of the layer containing sulphur The film quality of the oleoresin mixture reaches 5% of the total mass of the final product environmentally friendly composite coated slow release urea. Then, stop spraying the tung oil, and continue to spray about 150 熔融 of molten sulfur on the surface of the sulfur-containing tung oil resin mixture film layer until the quality of the formed sulfur film layer reaches 8% of the total mass of the final product environmentally friendly composite coated type slow-release urea. Then, a benzene solution of a polyethylene wax having a molecular weight of 1500 is sprayed on the surface of the sulfur film layer until the quality of the formed polyethylene wax film layer reaches 1.5% of the total mass of the final product environmentally friendly composite coated slow release urea, and the benzene is sufficiently dried to remove benzene. . Finally, slowly spray sulphur-containing tung oil on the surface of the polyethylene wax film (containing 0.4% of the tung oil quality, sulphur: tung oil mass ratio is 1:1) until the formed sulfur-containing tung oil resin mixture film layer The quality reaches 4% of the total quality of the finished product environmentally friendly composite coated slow release urea. The tung oil resin in the film layer is sufficiently cured to obtain an environmentally friendly composite film type slow release urea. The release period of the prepared environmentally-friendly composite coated slow release urea was 203 days.
实施例 10 Example 10
将粒径为 2.0〜4.0mm的粒状工业尿素加入流化床包膜设备中, 并使粒状尿素处于 沸腾状态, 流化床中粒状尿素温度保持在 75°C。 将含硫磺的三聚氰胺一甲醛树脂预聚 物水溶液 (三聚氰胺一甲醛树脂预聚物是三聚氰胺:甲醛摩尔比为 1: 3.2的三聚氰胺 与甲醛反应所制备, 硫磺:三聚氰胺一甲醛树脂预聚物之质量比为 7: 3 ) 喷涂于尿素 表面, 直到形成的该层含硫三聚氰胺一甲酸树脂混合物膜层质量达到最终成品环保复 合包膜型缓释尿素总质量的 4%, 干燥除去膜层中含水。 随后, 在含硫三聚氰胺一甲醛 树脂混合物膜层表面慢慢喷涂 150°C左右熔融硫磺,直到形成的硫磺膜层质量达到最终 成品环保复合包膜型缓释尿素总质量的 6%。 然后, 流化床中粒状尿素温度降至 60°C, 再喷涂温度为 90°C的石蜡(熔点 75°C )熔体在硫磺膜层表面, 直到形成的石蜡膜层质 量达到最终成品环保复合包膜型缓释尿素总质量的 2%。最后, 再在石蜡膜层表面喷涂 桐油 (含有桐油质量 0.4%的催干剂), 直到形成的桐油树脂膜层质量达到最终成品环 保复合包膜型缓释尿素总质量的 2%。使膜层中的三聚氰胺一甲酸树脂和桐油树脂固化 充分, 即得环保复合包膜型缓释尿素。 所制得的环保复合包膜型缓释尿素的释放期为 197天。 Granular industrial urea having a particle size of 2.0 to 4.0 mm is introduced into the fluidized bed coating apparatus, and the granular urea is in a boiling state, and the temperature of the granular urea in the fluidized bed is maintained at 75 °C. A sulphur-containing melamine-formaldehyde resin prepolymer aqueous solution (melamine-formaldehyde resin prepolymer is prepared by reacting melamine with formaldehyde in a molar ratio of 1:3.2, and sulfur: melamine-formaldehyde resin prepolymer) 7: 3) Sprayed on the urea surface until the formed layer of the sulfur-containing melamine-formic acid resin mixture has a film quality of 4% of the total mass of the final product environmentally friendly composite coated slow release urea, and the water is removed by drying. Subsequently, the surface of the sulfur-containing melamine-formaldehyde resin mixture film layer is slowly sprayed with molten sulfur at a temperature of about 150 ° C until the quality of the formed sulfur film layer reaches 6% of the total mass of the final product environmentally friendly composite coated slow release urea. Then, the temperature of the granular urea in the fluidized bed is lowered to 60 ° C, and the paraffin wax (melting point 75 ° C) at a temperature of 90 ° C is sprayed on the surface of the sulfur film layer until the quality of the formed paraffin film layer reaches the final product environmentally friendly compound. 2% of the total mass of the coated slow release urea. Finally, tung oil (containing a drier of 0.4% tung oil) was sprayed on the surface of the paraffin layer until the quality of the tung oil resin film reached 2% of the total mass of the final product-encapsulated composite coated slow-release urea. The melamine-carboxylic acid resin and the tung oil resin in the film layer are sufficiently cured to obtain an environmentally-friendly composite film-type slow-release urea. The release period of the environmentally friendly composite coated slow release urea was 197 days.
实施例 11 Example 11
将粒径为 2.0~4.0mm的粒状工业尿素加入流化床包膜设备中, 并使粒状尿素处于 沸腾状态, 流化床中粒状尿素温度保持在 75°C。 将含硫磺的三聚氰胺一甲醛树脂预聚 物水溶液(三聚氰胺一甲醛树脂预聚物是三聚氰胺:甲醛摩尔比为 1: 3.2的三聚氰胺 与甲醛反应所制备, 硫磺:三聚氰胺一甲醛树脂预聚物之质量比为 7: 3 ) 喷涂于尿素 表面, 直到形成的该层含硫三聚氰胺一甲醛树脂混合物膜层质量达到最终成品环保复 合包膜型缓释尿素总质量的 4%, 干燥除去膜层中含水。 随后, 在含硫三聚氰胺一甲醛 树脂混合物膜层表面慢慢喷涂 150°C左右熔融硫磺,直到形成的硫磺膜层质量达到最终 成品环保复合包膜型缓释尿素总质量的 6%。 然后, 流化床中粒状尿素温度降至 65°C, 再喷涂温度为 95Ό的石蜡与松香混合物 (混合物熔点 80°C,石蜡:松香之质量比为 2: 1 )熔体在硫磺膜层表面, 直到形成的石蜡与松香混合物膜层质量达到最终成品环保复 合包膜型缓释尿素总质量的 2%。最后, 再在石蜡与松香混合物膜层表面喷涂桐油(含 有桐油质量 0.4%的催干剂), 直到形成的桐油树脂膜层质量达到最终成品环保复合包 膜型缓释尿素总质量的 2%。使膜层中的三聚氤胺—甲醛树脂和桐油树脂固化充分, 即 得环保复合包膜型缓释尿素。 所制得的环保复合包膜型缓释尿素的释放期为 158天。 The granular industrial urea having a particle diameter of 2.0 to 4.0 mm is introduced into the fluidized bed coating device, and the granular urea is in a boiling state, and the temperature of the granular urea in the fluidized bed is maintained at 75 °C. A sulphur-containing melamine-formaldehyde resin prepolymer aqueous solution (melamine-formaldehyde resin prepolymer is prepared by reacting melamine with formaldehyde in a molar ratio of 1:3.2, and sulfur: melamine-formaldehyde resin prepolymer) 7: 3) Sprayed on the urea surface until the formed layer of the sulfur-containing melamine-formaldehyde resin mixture reaches 4% of the total mass of the final product environmentally friendly composite coated slow release urea, and the water is removed by drying. Subsequently, the surface of the film layer of the sulfur-containing melamine-formaldehyde resin mixture is slowly sprayed with molten sulfur at a temperature of about 150 ° C until the quality of the formed sulfur film layer reaches the final. 6% of the total quality of the finished environmentally friendly composite coated slow release urea. Then, the temperature of the granular urea in the fluidized bed is lowered to 65 ° C, and the mixture of paraffin and rosin having a temperature of 95 喷涂 is sprayed (the mixture has a melting point of 80 ° C, and the paraffin: rosin mass ratio is 2:1). The melt is melted on the surface of the sulfur film layer. Until the formation of the paraffin and rosin mixture film quality reaches 2% of the total quality of the final product environmentally friendly composite coated slow release urea. Finally, the surface of the paraffin and rosin mixture film was sprayed with tung oil (containing 0.4% of tung oil quality drier) until the quality of the tung oil resin film layer reached 2% of the total quality of the final product environmentally friendly composite coated slow release urea. The trimeric guanamine-formaldehyde resin and the tung oil resin in the film layer are fully cured, that is, the environmentally friendly composite coated type sustained-release urea is obtained. The release period of the prepared environmentally-friendly composite coated slow release urea was 158 days.
实施例 12 Example 12
将粒径为 2.0〜4.0mm的粒状工业尿素加入控温 75°C的转鼓包膜设备中, 转动转鼓 (转速 40r/min) 使粒状尿素在转鼓内流动。 将顺丁橡胶生胶(牌号 BR9175型)苯溶 液喷涂在粒状尿素表面, 直到形成的顺丁橡胶生胶膜层质量达到最终成品环保复合包 膜型缓释尿素总质量的 1%, 充分千燥除去溶剂苯。 然后, 将 150°C熔融硫磺慢慢喷涂 于顺丁橡胶生胶膜层表面, 直到形成的硫磺膜层质量达到最终成品环保复合包膜型缓 释尿素总质量的 8%。然后, 再在硫磺膜层表面喷涂含硫磺的聚乙烯醇缩甲醛树脂(聚 乙烯醇牌号为 1799型、 缩醛度为 85%)溶液(溶剂为乙醇-甲苯混合溶剂, 硫磺:聚 乙烯醇缩甲醛树脂之质量比为 7: 3),直到形成的含硫聚乙烯醇缩甲醛树脂混合物膜层 质量达到最终成品环保复合包膜型缓释尿素总质量的 7%。充分干燥除去溶剂, 使聚乙 烯醇缩甲醛树脂充分固化, 即得环保复合包膜型缓释尿素。 所制得的环保复合包膜型 缓释尿素的释放期为 167天。 The granular industrial urea having a particle diameter of 2.0 to 4.0 mm was placed in a drum coating apparatus controlled at a temperature of 75 ° C, and the rotating drum (rotation speed of 40 r/min) was caused to flow the granular urea in the drum. Spraying butyl rubber (grade BR9175) benzene solution on the surface of granular urea until the quality of the formed butadiene rubber film reaches 1% of the total quality of the final product environmentally friendly composite coated slow release urea. The solvent benzene was removed. Then, 150 ° C molten sulfur was slowly sprayed on the surface of the butadiene rubber raw rubber film layer until the quality of the formed sulfur film layer reached 8% of the total mass of the final product environmentally friendly composite coated type slow release urea. Then, a sulfur-containing polyvinyl formal resin (polyvinyl alcohol grade 1799, 85% acetal) solution is sprayed on the surface of the sulfur film layer (the solvent is an ethanol-toluene mixed solvent, sulfur: polyvinyl alcohol The mass ratio of the formaldehyde resin is 7:3) until the film quality of the formed sulfur-containing polyvinyl formal resin mixture reaches 7% of the total mass of the final product environmentally friendly composite coated slow release urea. The solvent is sufficiently dried to completely cure the polyvinyl acetal resin, thereby obtaining an environmentally friendly composite coated slow release urea. The release period of the environmentally friendly composite coated slow release urea was 167 days.
实施例 13 Example 13
将粒径为 2.0~4.0mm的粒状工业尿素加入流化床包膜设备中, 并使粒状尿素处于 沸腾状态, 流化床中粒状尿素温度保持在 70°C。 将 150Ό左右熔融硫磺慢慢喷涂于尿 素表面, 直到形成的硫磺膜层质量达到最终成品环保复合包膜型缓释尿素总质量的 9%。 然后, 将苯乙烯一丁二烯一苯乙烯嵌段共聚物 (SBS, 牌号 raton D1101 ) 环己 垸溶液喷涂在硫磺膜层表面, 直到形成的苯乙烯一丁二烯一苯乙烯嵌段共聚物膜层质 量达到最终成品环保复合包膜型缓释尿素总质量的 1%, 充分干燥除去溶剂。然后, 再 在苯乙烯一丁二烯一苯乙烯嵌段共聚物膜层表面喷涂硝酸纤维素溶液(溶剂为乙醇、 丙酮和乙酸戊酯三者的混合溶剂),直到形成的硝酸纤维素膜层质量达到最终成品环保 复合包膜型缓释尿素总质量的 3%。干燥除去膜层中溶剂, 即得环保复合包膜型缓释尿 素。 所制得的环保复合包膜型缓释尿素的释放期为 157天。 The granular industrial urea having a particle diameter of 2.0 to 4.0 mm is introduced into the fluidized bed coating device, and the granular urea is in a boiling state, and the temperature of the granular urea in the fluidized bed is maintained at 70 °C. About 150 熔融 of molten sulfur is slowly sprayed on the surface of the urea until the quality of the formed sulfur film reaches 9% of the total mass of the final product environmentally friendly composite coated slow release urea. Then, a styrene-butadiene-styrene block copolymer (SBS, grade raton D1101) cyclohexanide solution is sprayed on the surface of the sulfur film layer until the formed styrene-butadiene-styrene block copolymer The film quality reaches 1% of the total mass of the final product environmentally friendly composite coated slow release urea, and the solvent is sufficiently dried. Then, a nitrocellulose solution (the solvent is a mixed solvent of ethanol, acetone and amyl acetate) is sprayed on the surface of the styrene-butadiene-styrene block copolymer film layer until the formed nitrocellulose film layer The quality reaches 3% of the total quality of the final finished environmentally friendly composite coated slow release urea. The solvent in the film layer is removed by drying to obtain an environmentally friendly composite coated slow release urea. The release period of the environmentally friendly composite coated slow release urea was 157 days.
实施例 14 Example 14
将粒径为 2.0〜4.0mm的粒状工业尿素加入流化床包膜设备中, 并使粒状尿素处于 沸腾状态, 流化床中粒状尿素温度保持在 90°C。 将含硫磺的三聚氰胺一甲醛树脂预聚 物水溶液(三聚氰胺一甲醛树脂预聚物是三聚氰胺:甲醛摩尔比为 1: 2.7的三聚氰胺 与甲醛反应所制备, 硫磺:三聚氰胺一甲醛树脂预聚物之质量比为 1: 1 ) 喷涂于尿素 表面, 直到形成的该层含硫三聚氰胺一甲醛树脂混合物膜层质量达到最终成品环保复 合包膜型缓释尿素总质量的 2%, 干燥除去膜层中含水。然后, 再在含硫三聚氰胺一甲 醛树脂混合物膜层表面慢慢喷涂 150°C左右熔融硫磺,直到形成的硫磺膜层质量达到最 终成品环保复合包膜型缓释尿素总质量的 10%。 最后, 再在硫磺膜层表面喷涂含硫磺 的三聚氰胺一甲醛树脂预聚物水溶液(三聚氰胺一甲醛树脂预聚物是三聚氰胺:甲醛 摩尔比为 1: 3的三聚氰胺与甲醛反应所制备,硫磺:三聚氰胺一甲醛树脂预聚物之质 量比为 2: 3),直到形成的该层含硫三聚氰胺一甲醛树脂混合物膜层质量达到最终成品 环保复合包膜型缓释尿素总质量的 6%。干燥除去膜层中含水, 并使膜层中的三聚氰胺 一甲醛树脂固化充分, 即得环保复合包膜型缓释尿素。 所制得的环保复合包膜型缓释 尿素的释放期为 131天。 Adding granular industrial urea with a particle size of 2.0~4.0mm into the fluidized bed coating equipment, and placing the granular urea in In the boiling state, the temperature of the granular urea in the fluidized bed is maintained at 90 °C. A sulphur-containing melamine-formaldehyde resin prepolymer aqueous solution (melamine-formaldehyde resin prepolymer is prepared by reacting melamine:melamine with a formaldehyde molar ratio of 1:2.7, and sulfur: melamine-formaldehyde resin prepolymer) Sprayed on the urea surface for 1:1) until the formed layer of the sulfur-containing melamine-formaldehyde resin mixture reaches 2% of the total mass of the final product environmentally friendly composite coated slow-release urea, and the water is removed by drying. Then, the surface of the sulfur-containing melamine-formaldehyde resin mixture film layer is slowly sprayed with molten sulfur at a temperature of about 150 ° C until the quality of the formed sulfur film layer reaches 10% of the total mass of the final product environmentally friendly composite coated slow release urea. Finally, a sulphur-containing melamine-formaldehyde resin prepolymer aqueous solution is sprayed on the surface of the sulfur film layer (melamine-formaldehyde resin prepolymer is prepared by reacting melamine with formaldehyde in a molar ratio of 1:3, and melamine: melamine The mass ratio of the formaldehyde resin prepolymer is 2:3) until the film quality of the layer of the sulfur-containing melamine-formaldehyde resin mixture formed reaches 6% of the total mass of the final product environmentally friendly composite coated slow release urea. The water is removed from the film layer by drying, and the melamine-formaldehyde resin in the film layer is sufficiently cured to obtain an environmentally friendly composite coated type slow-release urea. The release period of the prepared environmentally-friendly composite coated slow release urea was 131 days.
实施例 15 Example 15
将粒径为 2.0~4.0mm的粒状工业尿素加入流化床包膜设备中, 并使粒状尿素处于 沸腾状态, 流化床中粒状尿素温度保持在 90Ό。 在粒状尿素表面喷涂含硫磺的脲醛树 脂预聚物水溶液(脲醛树脂预聚物是尿素:甲醛摩尔比为 1: 2的尿素与甲醛反应所制 备,硫磺:脲醛树脂预聚物之质量比为 3: 2),直到形成的该层含硫脲醛树脂混合物膜 层质量达到最终成品环保复合包膜型缓释尿素总质量的 6%,干燥除去膜层中含水。然 后,将 150°C熔融硫磺慢慢喷涂于含硫脲醛树脂混合物膜层表面,直到形成的硫磺膜层 质量达到最终成品环保复合包膜型缓释尿素总质量的 10%。 然后, 再在硫磺膜层表面 喷涂含硫磺的脲醛树脂预聚物水溶液(脲醛树脂预聚物是尿素:甲醛摩尔比为 1: 1.5 的尿素与甲醛反应所制备,硫磺:脲醛树脂预聚物之质量比为 1: 3),直到形成的该层 含硫脲醛树脂混合物膜层质量达到最终成品环保复合包膜型缓释尿素总质量的 2%。干 燥除去膜层中含水, 并使膜层中的脲醛树脂固化充分, 即得环保复合包膜型缓释尿素。 所制得的环保复合包膜型缓释尿素的释放期为 115天。 The granular industrial urea with a particle size of 2.0~4.0mm is added to the fluidized bed coating equipment, and the granular urea is in a boiling state, and the granular urea temperature in the fluidized bed is maintained at 90 Ό. Spraying a sulfur-containing urea-formaldehyde resin prepolymer aqueous solution on the surface of granular urea (urea resin prepolymer is prepared by reacting urea with formaldehyde in a molar ratio of 1:2, and formaldehyde: the mass ratio of sulfur: urea-formaldehyde resin prepolymer is 3 2), until the formed layer of the thiourea-containing resin mixture film layer reaches 6% of the total mass of the final product environmentally friendly composite coated type slow-release urea, and the water is removed by drying. Then, molten sulfur at 150 ° C is slowly sprayed onto the surface of the film layer containing the thiourea resin mixture until the quality of the sulfur film layer formed reaches 10% of the total mass of the final product environmentally friendly composite coated slow release urea. Then, a sulfur-containing urea-formaldehyde resin prepolymer aqueous solution is sprayed on the surface of the sulfur film layer (the urea-formaldehyde resin prepolymer is prepared by reacting urea with a formaldehyde molar ratio of 1:1.5 and formaldehyde, and sulfur: urea-formaldehyde resin prepolymer) The mass ratio is 1:3) until the film quality of the layer containing the thiourea resin mixture is 2% of the total mass of the final product environmentally friendly composite coated slow release urea. The water is removed from the film layer, and the urea-formaldehyde resin in the film layer is sufficiently cured to obtain an environmentally-friendly composite film-type slow-release urea. The release period of the environmentally friendly composite coated slow release urea was 115 days.
实施例 16 Example 16
将粒径为 2.0~4.0mm的粒状工业尿素加入流化床包膜设备中, 并使粒状尿素处于 沸腾状态, 流化床中粒状尿素温度保持在 80°C。 将三聚氰胺一甲醛树脂预聚物水溶液 (三聚氰胺一甲醛树脂预聚物是三聚氰胺:甲醛摩尔比为 1: 3的三聚氰胺与甲醛反应 所制备) 和 150Ό左右的熔融硫磺分别从两组不同的喷嘴同时往粒状尿素表面慢慢喷 涂, 通过控制它们的喷涂流量比, 使形成的含硫三聚氰胺一甲醛树脂混合物膜层中硫 磺的平均质量分数为 70%, 直到形成的该层含硫三聚氰胺一甲醛树脂混合物膜层质量 达到最终成品环保复合包膜型缓释尿素总质量的 3%, 干燥除去膜层中含水。然后, 停 止喷涂三聚氰胺一甲醛树脂预聚物水溶液,继续慢慢喷涂 150°C左右熔融硫磺在含硫三 聚氰胺一甲醛树脂混合物膜层表面, 直到形成的硫磺膜层质量达到最终成品环保复合 包膜型缓释尿素总质量的 3.5%。 最后, 再在硫磺膜层表面喷涂含硫磺的三聚氰胺一甲 醛树脂预聚物水溶液(三聚氰胺一甲醛树脂预聚物是三聚氰胺:甲醛摩尔比为 1: 3的 三聚氰胺与甲醛反应所制备,硫磺:三聚氰胺一甲醛树脂预聚物之质量比为 1: 1 ),直 到形成的该层含硫三聚氮胺一甲醛树脂混合物膜层质量达到最终成品环保复合包膜型 缓释尿素总质量的 2%。充分干燥除去膜层中含水, 并使膜层中的三聚氰胺一甲醛树脂 固化充分, 即得环保复合包膜型缓释尿素。 所制得的环保复合包膜型缓释尿素的释放 期为 56天。 The granular industrial urea having a particle diameter of 2.0 to 4.0 mm is introduced into the fluidized bed coating device, and the granular urea is in a boiling state, and the temperature of the granular urea in the fluidized bed is maintained at 80 °C. A melamine-formaldehyde resin prepolymer aqueous solution (melamine-formaldehyde resin prepolymer is prepared by reacting melamine: melamine with a formaldehyde molar ratio of 1:3) and about 150 Å of molten sulfur from two different nozzles simultaneously The surface of the granular urea is slowly sprayed, and the sulfur content in the formed sulfur-containing melamine-formaldehyde resin mixture layer is controlled by controlling the spray flow ratio thereof. The average mass fraction of the sulfonate is 70% until the formed film layer of the sulfur-containing melamine-formaldehyde resin mixture reaches 3% of the total mass of the final product environmentally friendly composite coated slow release urea, and the water is removed by drying. Then, stop spraying the melamine-formaldehyde resin prepolymer aqueous solution, and continue to spray the molten sulfur at a temperature of about 150 ° C on the surface of the sulfur-containing melamine-formaldehyde resin mixture film layer until the quality of the formed sulfur film layer reaches the final product environmentally friendly composite coating type. 3.5% of the total mass of slow release urea. Finally, a sulphur-containing melamine-formaldehyde resin prepolymer aqueous solution is sprayed on the surface of the sulfur film layer (melamine-formaldehyde resin prepolymer is prepared by reacting melamine with formaldehyde in a molar ratio of 1:3, and melamine: melamine The mass ratio of the formaldehyde resin prepolymer is 1:1) until the film quality of the layer of the sulfur-containing triazide-formaldehyde resin mixture formed reaches 2% of the total mass of the final product environmentally friendly composite coated slow release urea. The melamine-formaldehyde resin in the film layer is sufficiently dried by sufficiently drying to remove water in the film layer, thereby obtaining an environmentally friendly composite coated type slow-release urea. The release period of the environmentally friendly composite coated slow release urea prepared was 56 days.
实施例 17 Example 17
将粒径为 2.0〜4.0mm的粒状工业尿素加入流化床包膜设备中, 并使粒状尿素处于 沸腾状态, 流化床中粒状尿素温度保持在 90°C。 将 150Ό左右熔融硫磺慢慢喷涂于尿 素表面, 直到硫磺膜层质量达到最终成品环保复合包膜型缓释尿素总质量的 10%。 然 后, 在硫磺膜层上喷涂含硫磺的三聚氰胺一甲醛树脂预聚物水溶液 (三聚氰胺一甲醛 树脂预聚物是三聚氰胺:甲醛摩尔比为 1: 3的三聚氰胺与甲醛反应所制备,硫磺:三 聚氰胺一甲醛树脂预聚物之质量比为 3: 2),直到形成的含硫三聚氰胺一甲醛树脂混合 物膜层质量达到最终成品环保复合包膜型缓释尿素总质量的 4%。 千燥除去膜层中含 水, 并使膜层中的三聚氰胺一甲醛树脂固化充分, 即得环保复合包膜型缓释尿素。 所 制得的环保复合包膜型缓释尿素的释放期为 75天。 Granular industrial urea having a particle size of 2.0 to 4.0 mm is introduced into the fluidized bed coating apparatus, and the granular urea is in a boiling state, and the temperature of the granular urea in the fluidized bed is maintained at 90 °C. About 150 熔融 of molten sulfur is slowly sprayed on the surface of the urea until the quality of the sulfur film reaches 10% of the total mass of the final product environmentally friendly composite coated slow release urea. Then, a sulphur-containing melamine-formaldehyde resin prepolymer aqueous solution is sprayed on the sulfur film layer (melamine-formaldehyde resin prepolymer is prepared by reacting melamine with a formaldehyde molar ratio of 1:3, and melamine: melamine-formaldehyde The mass ratio of the resin prepolymer is 3: 2) until the film quality of the formed sulfur-containing melamine-formaldehyde resin mixture reaches 4% of the total mass of the final product environmentally friendly composite coated slow release urea. The water is removed from the film layer, and the melamine-formaldehyde resin in the film layer is sufficiently cured to obtain an environmentally-friendly composite film-type slow-release urea. The release period of the environmentally friendly composite coated slow release urea was 75 days.
实施例 18 Example 18
将粒径为 2.0~4.0mm的粒状工业尿素加入流化床包膜设备中, 并使粒状尿素处于 沸腾状态, 流化床中粒状尿素温度保持在 70T:。 将含硫磺的三聚氰胺一甲醛树脂预聚 物水溶液(三聚氰胺一甲醛树脂预聚物是三聚氰胺:甲醛摩尔比为 1: 3的三聚氰胺与 甲醛反应所制备, 硫磺:三聚氰胺一甲醛树脂预聚物之质量比为 7: 3 ) 喷涂于尿素表 面, 直到形成的该层含硫三聚氰胺一甲醛树脂混合物膜层质量达到最终成品环保复合 包膜型缓释尿素总质量的 4%, 干燥除去膜层中含水。 随后, 在含硫三聚氰胺一甲醛树 脂混合物膜层表面慢慢喷涂 150°C左右熔融硫磺,直到形成的硫磺膜层质量达到最终成 品环保复合包膜型缓释尿素总质量的 6%。然后, 再将丙烯腈一丁二烯一苯乙烯共聚物 (兰州石化公司, 牌号 ABS— 301 )的苯溶液喷涂在硫磺膜层表面, 直到形成的丙烯腈 一丁二烯一苯乙烯共聚物膜层质量达到最终成品环保复合包膜型缓释尿素总质量的 1%。最后,再在丙烯腈一丁二烯一苯乙烯共聚物膜层表面喷涂桐油(含有桐油质量 0.4% 的催干剂),直到形成的桐油树脂膜层质量达到最终成品环保复合包膜型缓释尿素总质 量的 2%。使膜层中的三聚氰胺一甲醛树脂和桐油树脂固化充分, 即得环保复合包膜型 缓释尿素。 所制得的环保复合包膜型缓释尿素的释放期为 165天。 The granular industrial urea with a particle size of 2.0~4.0mm is added to the fluidized bed coating equipment, and the granular urea is in a boiling state, and the granular urea temperature in the fluidized bed is maintained at 70T:. A sulphur-containing melamine-formaldehyde resin prepolymer aqueous solution (melamine-formaldehyde resin prepolymer is prepared by reacting melamine: melamine having a molar ratio of 1:3 with formaldehyde, sulfur: melamine-formaldehyde resin prepolymer mass ratio 7: 3) Sprayed on the urea surface until the formed layer of the sulfur-containing melamine-formaldehyde resin mixture reaches 4% of the total mass of the final product environmentally friendly composite coated slow release urea, and the water is removed by drying. Subsequently, the surface of the sulfur-containing melamine-formaldehyde resin mixture film layer is slowly sprayed with molten sulfur at a temperature of about 150 ° C until the quality of the formed sulfur film layer reaches 6% of the total mass of the final product environmentally friendly composite coated slow release urea. Then, a benzene solution of acrylonitrile-butadiene-styrene copolymer (Lanzhou Petrochemical Company, brand ABS-301) is sprayed on the surface of the sulfur film layer until the formed acrylonitrile-butadiene-styrene copolymer film The layer quality reaches the total quality of the final product environmentally friendly composite coated slow release urea 1%. Finally, the surface of the acrylonitrile-butadiene-styrene copolymer film was sprayed with tung oil (containing 0.4% dregs of tung oil) until the quality of the tung oil resin film reached the final product environmentally friendly composite film type sustained release. 2% of the total mass of urea. The melamine-formaldehyde resin and the tung oil resin in the film layer are fully cured, that is, the environmentally-friendly composite coated type slow-release urea is obtained. The release period of the environmentally friendly composite coated slow release urea was 165 days.
实施例 19 Example 19
将粒径为 2.0~4.0min的粒状工业尿素加入流化床包膜设备中, 并使粒状尿素处于 沸腾状态, 流化床中粒状尿素温度保持在 90°C。 将三聚氰胺一甲醛树脂预聚物水溶液 (三聚氰胺一甲醛树脂预聚物是三聚氰胺:甲醛摩尔比为 1: 3.5的三聚氰胺与甲醛反 应所制备)慢慢喷涂在粒状尿素表面, 直到形成的该层三聚氰胺一甲醛树脂膜层质量 达到最终成品环保复合包膜型缓释尿素总质量的 1.5%。 然后, 从两组不同的喷嘴同时 往三聚氰胺一甲醛树脂膜层表面分别慢慢喷涂三聚氰胺一甲醛树脂预聚物水溶液 (三 聚氰胺一甲醛树脂预聚物是三聚氰胺:甲醛摩尔比为 1: 2.5的三聚氰胺与甲醛反应所 制备)和 150°C左右的熔融硫磺,通过控制它们的喷涂流量比,使形成的含硫三聚氰胺 一甲醛树脂混合物膜层中硫磺的平均质量分数为 85%, 喷涂直到形成的该层含硫三聚 氰胺一甲醛树脂混合物膜层质量达到最终成品环保复合包膜型缓释尿素总质量的 4%, 干燥除去膜层中含水。 随后, 停止喷涂三聚氰胺一甲醛树脂预聚物水溶液, 继续慢慢 喷涂 150°C左右熔融硫磺,直到形成的硫磺膜层质量达到最终成品环保复合包膜型缓释 尿素总质量的 6%。然后,再在硫磺膜层表面喷涂含硫磺的三聚氰胺一甲醛树脂预聚物 水溶液(三聚氰胺一甲醛树脂预聚物是三聚氰胺:甲醛摩尔比为 1: 3的三聚氰胺与甲 醛反应所制备,硫磺:三聚氰胺一甲醛树脂预聚物之质量比为 7 : 3 ),直到形成的该层 含硫三聚氰胺一甲醛树脂混合物膜层质量达到最终成品环保复合包膜型缓释尿素总质 量的 3%。最后, 再在含硫三聚氰胺—甲醛树脂混合物膜层表面慢慢喷涂三聚氰胺一甲 醛树脂预聚物水溶液(三聚氰胺一甲醛树脂预聚物是三聚氰胺:甲醛摩尔比为 1: 2的 三聚氰胺与甲醛反应所制备),直到形成的该层三聚氰胺一甲酸树脂膜层质量达到最终 成品环保复合包膜型缓释尿素总质量的 1.5%。 干燥除去膜层中含水, 并使膜层中的三 聚氰胺一甲醛树脂固化充分, 即得环保复合包膜型缓释尿素。 所制得的环保复合包膜 型缓释尿素的释放期为 156天。 The granular industrial urea with a particle size of 2.0 to 4.0 min is added to the fluidized bed coating equipment, and the granular urea is in a boiling state, and the temperature of the granular urea in the fluidized bed is maintained at 90 °C. The melamine-formaldehyde resin prepolymer aqueous solution (melamine-formaldehyde resin prepolymer is prepared by reacting melamine:melamine with a formaldehyde molar ratio of 1:3.5 and formaldehyde) is slowly sprayed on the surface of the granular urea until the layer of melamine is formed. The quality of the formaldehyde resin film layer reaches 1.5% of the total quality of the final product environmentally friendly composite coated slow release urea. Then, the melamine-formaldehyde resin prepolymer aqueous solution is sprayed slowly from the two different nozzles to the surface of the melamine-formaldehyde resin film layer (melamine-formaldehyde resin prepolymer is melamine: melamine with a molar ratio of 1:2.5) The formaldehyde produced by the formaldehyde reaction) and the molten sulfur at about 150 ° C, by controlling the spray flow ratio thereof, the average mass fraction of sulfur in the formed sulfur-containing melamine-formaldehyde resin mixture layer is 85%, and spraying until the layer is formed. The film quality of the sulfur-containing melamine-formaldehyde resin mixture reaches 4% of the total mass of the final product environmentally friendly composite coated slow release urea, and the water is removed by drying. Subsequently, the spraying of the melamine-formaldehyde resin prepolymer aqueous solution is stopped, and the molten sulfur is continuously sprayed at about 150 ° C until the quality of the formed sulfur film layer reaches 6% of the total mass of the final product environmentally friendly composite coated slow release urea. Then, a sulphur-containing melamine-formaldehyde resin prepolymer aqueous solution is sprayed on the surface of the sulfur film layer (melamine-formaldehyde resin prepolymer is prepared by reacting melamine: melamine having a molar ratio of 1:3 with formaldehyde, sulfur: melamine one The mass ratio of the formaldehyde resin prepolymer is 7:3) until the film quality of the layer of the sulfur-containing melamine-formaldehyde resin mixture formed reaches 3% of the total mass of the final product environmentally friendly composite coated slow release urea. Finally, a melamine-formaldehyde resin prepolymer aqueous solution is slowly sprayed on the surface of the sulfur-containing melamine-formaldehyde resin mixture film layer (melamine-formaldehyde resin prepolymer is prepared by reacting melamine with a formaldehyde molar ratio of 1:2 and formaldehyde). ), until the formation of the layer of melamine-formic acid resin film layer quality reached 1.5% of the total quality of the final product environmentally friendly composite coated slow release urea. The water is removed from the film layer by drying, and the melamine-formaldehyde resin in the film layer is sufficiently cured to obtain an environmentally friendly composite coated type slow-release urea. The release period of the environmentally friendly composite coated slow release urea was 156 days.
实施例 20 Example 20
将 8x3^1的片状尿素加入流化床包膜设备中, 并使片状尿素处于沸腾状态, 流 化床中片状尿素温度保持在 90°C。 将三聚氰胺一甲醛树脂预聚物水溶液(三聚氰胺一 甲醛树脂预聚物是三聚氰胺:甲醛摩尔比为 1: 2.6的三聚氰胺与甲醛反应所制备) 和 150°C左右的瑢融硫磺分别从两组不同的喷嘴同时往片状尿素表面慢慢喷涂,通过控制 它们的喷涂流量比, 使形成的含硫三聚氰胺一甲醛树脂混合物膜层中硫磺的平均质量 分数为 70%, 喷涂直到形成的该层含硫三聚氰胺一甲醛树脂混合物膜层质量达到最终 成品环保复合包膜型缓释尿素总质量的 5%, 干燥除去膜层中含水。然后, 停止喷涂三 聚氰胺一甲醛树脂预聚物水溶液,继续慢慢喷涂 150°C熔融硫磺于含硫三聚氰胺一甲醛 树脂混合物膜层表面, 直到形成的硫磺膜层质量达到最终成品环保复合包膜型缓释尿 素总质量的 15%。 然后, 再在硫磺膜层表面喷涂含硫磺的三聚氰胺一甲醛树脂预聚物 水溶液(三聚氰胺一甲醛树脂预聚物是三聚氰胺:甲醛摩尔比为 1: 3的三聚氰胺与甲 醛反应所制备,硫磺:三聚氰胺一甲醛树脂预聚物之质量比为 1 : 1 ),直到形成的该层 含硫三聚氰胺一甲醛树脂混合物膜层质量达到最终成品环保复合包膜型缓释尿素总质 量的 5%。干燥除去膜层中含水, 并使膜层中的三聚氰胺一甲醛树脂固化充分, 即得环 保复合包膜型缓释尿素。 所制得的环保复合包膜型缓释尿素的释放期为 245天。 8 x 3 ^ 1 of flaky urea was added to the fluidized bed coating apparatus, and the flaky urea was placed in a boiling state, and the temperature of the flaky urea in the fluidized bed was maintained at 90 ° C. A melamine-formaldehyde resin prepolymer aqueous solution (melamine-formaldehyde resin prepolymer is prepared by reacting melamine with a formaldehyde molar ratio of 1:2.6 and melamine) and a sulphur sulphur at a temperature of about 150 ° C are respectively different from the two groups. The nozzle is slowly sprayed onto the surface of the flaky urea at the same time. Their spraying flow ratio is such that the average mass fraction of sulfur in the formed sulfur-containing melamine-formaldehyde resin mixture layer is 70%, and the quality of the layer of the sulfur-containing melamine-formaldehyde resin mixture formed until the formation reaches the final finished environmentally friendly composite package. 5% of the total mass of the membrane type slow-release urea, drying to remove water in the film layer. Then, stop spraying the melamine-formaldehyde resin prepolymer aqueous solution, and continue to spray 150 ° C molten sulfur on the surface of the sulfur-containing melamine-formaldehyde resin mixture film layer until the quality of the formed sulfur film layer reaches the final product environmentally friendly composite coating type. Release 15% of the total quality of urea. Then, a sulphur-containing melamine-formaldehyde resin prepolymer aqueous solution is sprayed on the surface of the sulfur film layer (melamine-formaldehyde resin prepolymer is prepared by reacting melamine with formaldehyde in a molar ratio of 1:3, and melamine: melamine The mass ratio of the formaldehyde resin prepolymer is 1:1) until the film quality of the layer of the sulfur-containing melamine-formaldehyde resin mixture formed reaches 5% of the total mass of the final product environmentally friendly composite coated slow release urea. The water is removed from the film layer by drying, and the melamine-formaldehyde resin in the film layer is sufficiently cured to obtain an environmentally friendly composite coated type slow-release urea. The release period of the prepared environmentally-friendly composite coated slow release urea was 245 days.
实施例 21 Example 21
将粒径为 2.0~4.0mm的粒状工业尿素加入控温 65°C的转鼓包膜设备中, 转动转鼓 (转速 40r/min)使粒状尿素在转鼓内流动。 将聚乙烯醇缩甲醛树脂(聚乙烯醇牌号为 1799型、缩醛度为 55%)溶液(溶剂为乙醇-甲苯混合溶剂)喷涂在粒状尿素表面, 直 到形成的聚乙烯醇缩甲醛树脂膜层质量达到最终成品环保复合包膜型缓释尿素总质量 的 3%, 充分干燥除去溶剂。 然后, 在聚乙烯醇缩甲醛树脂膜层表面慢慢喷涂 150°C熔 融硫磺, 直到形成的硫磺膜层质量达到最终成品环保复合包膜型缓释尿素总质量的 8%。 然后, 再在硫磺膜层表面喷涂聚乙烯醇缩丁醒树脂(聚乙烯醇牌号为 1799型、 缩醛度为 90%) 乙醇溶液, 直到形成的聚乙烯醇缩丁醛树脂膜层质量达到最终成品环 保复合包膜型缓释尿素总质量的 4%。充分干燥除去溶剂, 使聚乙烯醇缩甲 (丁)醛树 脂充分固化, 即得环保复合包膜型缓释尿素。 所制得的环保复合包膜型缓释尿素的释 放期为 106天。 The granular industrial urea with a particle size of 2.0 to 4.0 mm was placed in a drum coating device with a temperature control of 65 ° C, and the rotating drum (rotation speed 40 r / min) was used to flow the granular urea in the drum. Spraying a solution of polyvinyl formal resin (polyvinyl alcohol grade 1799, acetal degree 55%) on the surface of granular urea until the formed polyvinyl formal resin film layer The quality reaches 3% of the total mass of the final product environmentally friendly composite coated slow release urea, and the solvent is sufficiently dried. Then, 150 ° C of molten sulfur is slowly sprayed on the surface of the polyvinyl formal resin film layer until the quality of the formed sulfur film layer reaches 8% of the total mass of the final product environmentally friendly composite coated type slow release urea. Then, on the surface of the sulfur film layer, a polyvinyl alcohol shrinking resin (polyvinyl alcohol grade 1799, acetal degree 90%) ethanol solution is sprayed until the quality of the formed polyvinyl butyral resin film layer reaches the final. 4% of the total quality of the finished environmentally friendly composite coated slow release urea. The solvent is sufficiently dried to completely solidify the polyvinyl acetal resin, thereby obtaining an environmentally friendly composite coated slow release urea. The release period of the environmentally friendly composite coated slow release urea prepared was 106 days.
实施例 22 Example 22
将粒径为 2.0~4.0imn的粒状工业尿素加入流化床包膜设备中,并使粒状尿素处于沸 腾状态,流化床中粒状尿素温度保持在 90°C。将三聚氰胺改性脲醛树脂预聚物水溶液慢 慢喷涂在粒状尿素表面, 直到形成的该层三聚氰胺改性脲醛树脂膜层质量达到最终成品 环保复合包膜型缓释尿素总质量的 2%。 然后, 从两组不同的喷嘴同时往三聚氰胺改性 脲醛树脂膜层表面分别慢慢喷涂聚乙烯醇改性脲醛树脂预聚物水溶液和 150Ό左右熔融 硫磺, 通过控制它们的喷涂流量比, 使形成的含硫聚乙烯醇改性脲醛树脂混合物膜层中 硫磺的平均质量分数为 75%, 喷涂直到形成的该层含硫聚乙烯醇改性脲醛树脂混合物膜 层质量达到最终成品环保复合包膜型缓释尿素总质量的 3%, 干燥除去膜层中含水。 随 后,停止喷涂聚乙烯醇改性脲醛树脂预聚物水溶液,继续慢慢喷涂 150 C左右熔融硫磺, 直到形成的硫磺膜层质量达到最终成品环保复合包膜型缓释尿素总质量的 7%。 然后, 从两组不同的喷嘴同时往硫磺膜层表面慢慢喷涂乙醇改性三聚氰胺一甲醛树脂预聚物 水溶液和 150°C左右的熔融硫磺, 通过控制它们的喷涂流量比, 使形成的含硫乙醇改性 三聚氰胺一甲醛树脂混合物膜层中硫磺的平均质量分数为 65%, 喷涂直到形成的该层含 硫乙醇改性三聚氰胺一甲醛树脂混合物膜层质量达到最终成品环保复合包膜型缓释尿 素总质量的 2%。 最后, 再在含硫乙醇改性三聚氰胺一甲醛树脂混合物膜层表面慢慢喷 涂三聚氰胺一甲醛树脂预聚物水溶液(三聚氰胺一甲醛树脂预聚物是三聚氰胺:甲醛摩 尔比为 1: 1.5的三聚氰胺与甲醛反应所制备), 直到形成的该层三聚氰胺一甲醛树脂膜 层质量达到最终成品环保复合包膜型缓释尿素总质量的 2%。 干燥除去膜层中含水, 并 使膜层中的改性脲醛树脂和 (改性)三聚氰胺一甲醛树脂固化充分, 即得环保复合包膜 型缓释尿素。 所制得的环保复合包膜型缓释尿素的释放期为 160天。 The granular industrial urea with a particle size of 2.0~4.0imn is added to the fluidized bed coating equipment, and the granular urea is in a boiling state, and the granular urea temperature in the fluidized bed is maintained at 90 °C. The aqueous solution of the melamine-modified urea-formaldehyde resin prepolymer is slowly sprayed on the surface of the granular urea until the quality of the layer of the melamine-modified urea-formaldehyde resin layer reaches 2% of the total mass of the final product environmentally friendly composite coated slow-release urea. Then, from the two sets of different nozzles, the polyvinyl alcohol-modified urea-formaldehyde resin prepolymer aqueous solution and 150 Å of molten sulfur are sprayed on the surface of the melamine-modified urea-formaldehyde resin film layer simultaneously, and the spray flow ratio is controlled by controlling the spray flow ratio thereof. The average mass fraction of sulfur in the film layer of the sulfur-containing polyvinyl alcohol modified urea-formaldehyde resin mixture is 75%, and the quality of the film layer of the sulfur-containing polyvinyl alcohol-modified urea-formaldehyde resin mixture formed until the formation of the layer is the final product environmentally friendly composite film type Release 3% of the total mass of urea, dry to remove water in the film. With After that, the spraying of the polyvinyl alcohol-modified urea-formaldehyde resin prepolymer aqueous solution is stopped, and the molten sulfur is continuously sprayed for about 150 C until the quality of the formed sulfur film layer reaches 7% of the total mass of the final product environmentally friendly composite coated slow-release urea. Then, from the two sets of different nozzles, the ethanol-modified melamine-formaldehyde resin prepolymer aqueous solution and the molten sulfur at about 150 °C are sprayed slowly onto the surface of the sulfur film layer, and the sulfur content formed is controlled by controlling the spray flow ratio thereof. The average mass fraction of sulfur in the membrane of the ethanol-modified melamine-formaldehyde resin mixture is 65%, and the quality of the film layer of the melamine-modified melamine-formaldehyde resin mixture is reached until the final product of the environmentally friendly composite coating type slow-release urea is formed. 2% of the total mass. Finally, the melamine-formaldehyde resin prepolymer aqueous solution is slowly sprayed on the surface of the thiol-modified melamine-formaldehyde resin mixture film layer (melamine-formaldehyde resin prepolymer is melamine: melamine and formaldehyde with a molar ratio of 1:1.5) The reaction is prepared) until the quality of the layer of the melamine-formaldehyde resin layer formed reaches 2% of the total mass of the final product environmentally friendly composite coated slow release urea. The water in the film layer is removed by drying, and the modified urea-formaldehyde resin and the (modified) melamine-formaldehyde resin in the film layer are sufficiently cured to obtain an environmentally-friendly composite film-type slow-release urea. The release period of the environmentally friendly composite coated slow release urea prepared was 160 days.
实施例 23 Example 23
将粒径为 2.0~4.0mm的粒状工业尿素加入流化床包膜设备中, 并使粒状尿素处于 沸腾状态, 流化床中粒状尿素温度保持在 90°C。 将正丁醇改性脲酸树脂预聚物水溶液 和 150°C左右熔融硫磺分别从两组不同的喷嘴同时往尿素表面喷涂,通过控制它们的喷 涂流量比, 使形成的含硫正丁醇改性脲醛树脂混合物膜层中硫磺的平均质量分数为 80%, 喷涂直到形成的该层含硫正丁醇改性脲醛树脂混合物膜层质量达到最终成品环 保复合包膜型缓释尿素总质量的 4%, 干燥除去膜层中含水。 随后, 在含硫正丁醇改性 脲醛树脂混合物膜层表面慢慢喷涂 150°C左右熔融硫磺,直到形成的硫磺膜层质量达到 最终成品环保复合包膜型缓释尿素总质量的 6%。然后, 再在硫磺膜层表面喷涂含硫磺 的乙醇一聚乙烯醇改性三聚氰胺一甲醛树脂预聚物水溶液(硫磺:乙醇一聚乙烯醇改 性三聚氰胺一甲醛树脂预聚物之质量比为 7: 3),直到形成的该层含硫乙醇一聚乙烯醇 改性三聚氰胺一甲醛树脂混合物膜层质量达到最终成品环保复合包膜型缓释尿素总质 量的 4%。最后, 再在含硫乙醇一聚乙烯醇改性三聚氰胺一甲醛树脂混合物膜层表面喷 涂脲醛树脂预聚物水溶液 (脲醛树脂预聚物是尿素:甲醛摩尔比为 1: 1.05的尿素与甲 醛反应所制备),直到形成的该层脲醛树脂膜层质量达到最终成品环保复合包膜型缓释 尿素总质量的 1%。 干燥除去膜层中含水, 并使膜层中的(改性)脲醛树脂和改性三聚 氰胺一甲醛树脂固化充分, 即得环保复合包膜型缓释尿素。 所制得的环保复合包膜型 缓释尿素的释放期为 142天。 The granular industrial urea having a particle diameter of 2.0 to 4.0 mm is introduced into the fluidized bed coating device, and the granular urea is in a boiling state, and the temperature of the granular urea in the fluidized bed is maintained at 90 °C. The n-butanol-modified urethane resin prepolymer aqueous solution and the molten sulfur at about 150 °C are simultaneously sprayed from the two different nozzles to the urea surface, and the formed sulfur-containing n-butanol is changed by controlling the spray flow ratio thereof. The average mass fraction of sulfur in the film layer of the urea-formaldehyde resin mixture is 80%, and the film quality of the layer of sulfur-containing n-butanol-modified urea-formaldehyde resin mixture is up to 4, which is the total quality of the final product environmentally friendly composite coated type slow-release urea. %, dried to remove water in the film layer. Subsequently, the surface of the sulfur-containing n-butanol-modified urea-formaldehyde resin mixture film layer was slowly sprayed with molten sulfur at a temperature of about 150 ° C until the quality of the formed sulfur film layer reached 6% of the total mass of the final product environmentally friendly composite coated slow release urea. Then, a sulfur-containing ethanol-polyvinyl alcohol-modified melamine-formaldehyde resin prepolymer aqueous solution is sprayed on the surface of the sulfur film layer (the mass ratio of sulfur:ethanol-polyvinyl alcohol modified melamine-formaldehyde resin prepolymer is 7: 3), until the formation of the layer of sulfur-containing ethanol-polyvinyl alcohol modified melamine-formaldehyde resin mixture film layer quality reached 4% of the total quality of the final product environmentally friendly composite coated slow release urea. Finally, a urea-formaldehyde resin prepolymer aqueous solution is sprayed on the surface of the thiol-polyvinyl alcohol-modified melamine-formaldehyde resin mixture film layer (urea resin prepolymer is urea: formaldehyde molar ratio of 1:1.05 urea and formaldehyde reaction Prepared) until the quality of the layer of urea-formaldehyde resin film formed reaches 1% of the total mass of the final product environmentally friendly composite coated slow release urea. The water in the film layer is removed by drying, and the (modified) urea-formaldehyde resin and the modified melamine-formaldehyde resin in the film layer are sufficiently cured to obtain an environmentally friendly composite coated type slow-release urea. The release period of the environmentally friendly composite coated slow release urea was 142 days.
上述实施例中, 脲醛树脂预聚物水溶液是尿素与甲醛反应所制备, 尿素与甲醛摩尔 比可以在 1: ( 1~3 )范围,就所属专业领域的技术人员通常知识所知,通常以 1: ( 1~2) 为宜, 涂膜前加入脲醛树脂预聚物质量 2%的氯化铵固化剂。 三聚氰胺改性脲醛树脂 预聚物水溶液是尿素、三聚氰胺、 甲醛反应所制备, 尿素:三聚氰胺:甲醛摩尔比为 1 : 1 : 4, 涂膜前加入三聚氰胺改性脲醛树脂预聚物质量 2%的氯化铵固化剂。 聚乙烯 醇改性脲醛树脂预聚物水溶液是尿素、 甲醛、 聚乙烯醇反应所制备, 尿素:甲醛:聚 乙烯醇 (1799)质量比为 100: 89: 3, 涂膜前加入聚乙烯醇改性脲醛树脂预聚物质量 2%的氯化铵固化剂。 正丁醇改性脲醛树脂预聚物水溶液是尿素、 甲醛、 正丁醇反应所 制备, 尿素:甲醛:正丁醇摩尔比为 1: 1.37: 1, 涂膜前加入正丁醇改性脲醛树脂预 聚物质量 2%的氯化铵固化剂。 In the above embodiment, the urea-formaldehyde resin prepolymer aqueous solution is prepared by reacting urea with formaldehyde, and the molar ratio of urea to formaldehyde may be in the range of 1: (1~3), which is generally known by those skilled in the art, usually 1 : ( 1~2) Preferably, a 2% ammonium chloride curing agent having a urea resin resin prepolymer mass of 2% is added before the film coating. The melamine modified urea-formaldehyde resin prepolymer aqueous solution is prepared by the reaction of urea, melamine and formaldehyde. The urea:melamine:formaldehyde molar ratio is 1:1:4, and the melamine modified urea-formaldehyde resin prepolymer is added with 2% of the chlorine before the coating. Ammonium curing agent. The aqueous solution of polyvinyl alcohol modified urea-formaldehyde resin prepolymer is prepared by reacting urea, formaldehyde and polyvinyl alcohol. The ratio of urea:formaldehyde:polyvinyl alcohol (1799) is 100:89:3, and polyvinyl alcohol is added before coating. The urea-formaldehyde resin prepolymer has a 2% ammonium chloride curing agent. The n-butanol modified urea-formaldehyde resin prepolymer aqueous solution is prepared by the reaction of urea, formaldehyde and n-butanol. The urea:formaldehyde: n-butanol molar ratio is 1: 1.37: 1, and the n-butanol modified urea-formaldehyde resin is added before the film coating. Prepolymer mass 2% ammonium chloride curing agent.
上述实施例中,三聚氰胺一甲醛树脂预聚物水溶液是三聚氰胺与甲醛反应所制备, 三聚氰胺与甲醛摩尔比可以在 1: ( 1~4) 范围, 就所属专业领域的技术人员通常知识 所知, 通常以 1: ( 1.5~3.5)为宜, 涂膜前加入三聚氰胺一甲醛树脂预聚物质量 2%的 氯化铵或三乙醇铵固化剂。 乙醇改性三聚氰胺一甲醛树脂预聚物水溶液是三聚氛胺、 甲醛、 乙醇反应所制备, 三聚氰胺:甲醛:乙醇摩尔比为 1: 2.5: 2, 涂膜前加入乙醇 改性三聚氰胺一甲醛树脂预聚物质量 2%的氯化铵固化剂。乙醇一聚乙烯醇改性三聚氰 胺一甲醛树脂预聚物水溶液是三聚氰胺、 甲醛、 乙醇、 聚乙烯醇反应所制备, 三聚氰 胺:甲醛:乙醇:聚乙烯醇 (1788)质量比为 100: 67: 12: 2.5, 涂膜前加入乙醇一 聚乙烯醇改性三聚氰胺一甲醛树脂预聚物质量 2%的氯化铵固化剂。 In the above embodiment, the aqueous solution of the melamine-formaldehyde resin prepolymer is prepared by reacting melamine with formaldehyde, and the molar ratio of melamine to formaldehyde may be in the range of 1: (1~4), which is generally known to those skilled in the art, usually It is preferred to use 1: (1.5~3.5), and add 2% ammonium chloride or triethanolammonium curing agent of melamine-formaldehyde resin prepolymer before coating. The ethanol modified melamine-formaldehyde resin prepolymer aqueous solution is prepared by the reaction of trimeric amine, formaldehyde and ethanol. The melamine:formaldehyde:ethanol molar ratio is 1:2.5:2, and the ethanol modified melamine-formaldehyde resin is pre-coated before coating. 2% ammonium chloride curing agent. The ethanol-polyvinyl alcohol modified melamine-formaldehyde resin prepolymer aqueous solution is prepared by the reaction of melamine, formaldehyde, ethanol and polyvinyl alcohol, and the melamine:formaldehyde:ethanol:polyvinyl alcohol (1788) mass ratio is 100:67:12: 2.5, before the film coating, add ethanol-polyvinyl alcohol modified melamine-formaldehyde resin prepolymer mass 2% ammonium chloride curing agent.
就所属专业领域的技术人员通常知识所知, 改性脲醛树脂和改性三聚氰胺一甲醛 树脂分别属于脲醛树脂和三聚氰胺一甲醛树脂, 并且上述实施例中所采用的改性脲醛 树脂和改性三聚氰胺一甲醛树脂只分别是改性脲 '醛树脂和改性三聚氰胺一甲醛树脂的 个别代表, 所采用的改性脲酸树脂和改性三聚氰胺一甲醛树脂的制备配方也只是可采 用配方的个例, 并不对本发明构成范围限定。 氨基树脂中的三聚氰胺树脂除前述(改 性)三聚氰胺一甲醛树脂外, 可以采用乙二醛和糠醛等代替甲醛制备相应的三聚氰胺 树脂, 本说明书具体实施方式部分未列出相关实施例, 但是该类三聚氰胺树脂仍属于 本发明的发明范围。 As is known to those skilled in the art, the modified urea-formaldehyde resin and the modified melamine-formaldehyde resin are respectively a urea-formaldehyde resin and a melamine-formaldehyde resin, and the modified urea-formaldehyde resin and the modified melamine used in the above embodiments are The formaldehyde resin is only a representative of the modified urea 'aldehyde resin and the modified melamine-formaldehyde resin respectively. The preparation formula of the modified urethane resin and the modified melamine-formaldehyde resin can only be used as a formula, and The scope of the invention is not limited. The melamine resin in the amino resin may be prepared by using glyoxal and furfural instead of formaldehyde in addition to the above (modified) melamine-formaldehyde resin, and the related embodiments are not listed in the detailed description of the present specification, but such a class Melamine resins are still within the scope of the invention.
上述实施例中, 釆用的桐油是出自云南邱北、 酸值为 5.0mgKOH/g的市售桐油。 In the above examples, the tung oil used for the tanning is a commercially available tung oil from Qiubei, Yunnan, having an acid value of 5.0 mgKOH/g.
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| CN200510094058 | 2005-08-26 | ||
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| WO2007022732A1 true WO2007022732A1 (en) | 2007-03-01 |
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| Application Number | Title | Priority Date | Filing Date |
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| PCT/CN2006/002183 Ceased WO2007022732A1 (en) | 2005-08-26 | 2006-08-25 | A composite slow-release coated fertilizer without environmental pollution |
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Cited By (17)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US7771505B2 (en) * | 2008-07-16 | 2010-08-10 | Agrium Inc. | Controlled release fertilizer composition |
| WO2012025899A1 (en) | 2010-08-26 | 2012-03-01 | Dominó - Indústrias Cerâmicas Sa | Fragrance slow-release silica-based layer, ceramic tile and production process thereof |
| WO2012138210A1 (en) * | 2011-04-05 | 2012-10-11 | Universiti Teknologi Petronas | Multilayer controlled release fertilizer and method for producing the same |
| CN109265249A (en) * | 2018-10-31 | 2019-01-25 | 湖北富邦科技股份有限公司 | Delay the method for molten fertilizer for delaying the activator of molten object and using activator preparation |
| CN110981602A (en) * | 2019-12-17 | 2020-04-10 | 中盐安徽红四方肥业股份有限公司 | Coated slow-release fertilizer for rice and preparation method and application thereof |
| EP3693351A3 (en) * | 2014-05-05 | 2020-12-09 | SABIC Global Technologies B.V. | Coated granular fertilizers, methods of manufacture thereof, and uses |
| US11021409B2 (en) | 2017-08-09 | 2021-06-01 | Sabic Global Technologies B.V. | Extruded fertilizer granules with urease and/or nitrification inhibitors |
| US11104618B2 (en) | 2015-07-20 | 2021-08-31 | Sabic Global Technologies B.V. | Fertilizer composition and methods of making and using same |
| US11124463B2 (en) | 2015-11-16 | 2021-09-21 | Sabic Global Technologies B.V. | Coated granular fertilizers, methods of manufacture thereof, and uses thereof |
| CN113717010A (en) * | 2021-09-07 | 2021-11-30 | 新洋丰农业科技股份有限公司 | Preparation method of zinc efficient corn special fertilizer suitable for calcareous soil |
| CN114163284A (en) * | 2022-01-21 | 2022-03-11 | 黑龙江省昊千生物科技有限公司 | Flushing compound fertilizer uniformly applied by oil dispersion and production processing device thereof |
| US11306037B2 (en) | 2017-04-19 | 2022-04-19 | Sabic Global Technologies B.V. | Enhanced efficiency fertilizer with urease inhibitor and nitrification separated within the same particle |
| US11345645B2 (en) | 2017-04-20 | 2022-05-31 | Sabic Global Technologies B.V. | Enhanced efficiency fertilizer with embedded powder composition |
| US11358908B2 (en) | 2017-04-19 | 2022-06-14 | Sabic Global Technologies B.V. | Enhanced efficiency fertilizer with urease inhibitor and nitrification inhibitor in separate particles |
| CN115926347A (en) * | 2022-11-18 | 2023-04-07 | 河北工业大学 | Biodegradable mulching film for slow release of fertilizer and preparation method and application thereof |
| US11806689B2 (en) | 2016-02-08 | 2023-11-07 | Sabic Global Technologies B.V. | Method of making a fertilizer seed core |
| CN117859593A (en) * | 2024-03-12 | 2024-04-12 | 云南省农业科学院农业环境资源研究所 | Planting method for preventing and controlling bacterial wilt of continuous cropping tomatoes by using carbon-based biofertilizer |
Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH11228274A (en) * | 1998-02-09 | 1999-08-24 | Mitsui Touatsu Hiryo Kk | Sulfur-coated fertilizer |
| US5984994A (en) * | 1998-01-16 | 1999-11-16 | Hudson; Alice P. | Sulfur coated fertilizers with improved abrasion resistance |
| JP2001089284A (en) * | 1999-09-14 | 2001-04-03 | Mitsui Touatsu Hiryo Kk | Sulfur coated organic fertilizer |
| CN1465552A (en) * | 2002-07-04 | 2004-01-07 | �Ϻ���ͨ��ѧ | Film-coated slow-release fertilizer and preparation method thereof |
| CN1569774A (en) * | 2004-04-27 | 2005-01-26 | 山东农业大学 | Heavy polymer coated slow-release fertilizer with sulfide as bottom coat |
| CN1609063A (en) * | 2004-08-11 | 2005-04-27 | 吴成祥 | Slowly controlled releasing sulfur-containing urea and its prepn process |
| CN1634808A (en) * | 2003-12-26 | 2005-07-06 | 上海化工研究院 | Manufacturing method of sulfur-coated slow-release chemical fertilizer |
| CN1657512A (en) * | 2005-02-05 | 2005-08-24 | 方连明 | Release controlled coated fertilizer and its composition and preparation method |
-
2006
- 2006-08-25 WO PCT/CN2006/002183 patent/WO2007022732A1/en not_active Ceased
Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5984994A (en) * | 1998-01-16 | 1999-11-16 | Hudson; Alice P. | Sulfur coated fertilizers with improved abrasion resistance |
| JPH11228274A (en) * | 1998-02-09 | 1999-08-24 | Mitsui Touatsu Hiryo Kk | Sulfur-coated fertilizer |
| JP2001089284A (en) * | 1999-09-14 | 2001-04-03 | Mitsui Touatsu Hiryo Kk | Sulfur coated organic fertilizer |
| CN1465552A (en) * | 2002-07-04 | 2004-01-07 | �Ϻ���ͨ��ѧ | Film-coated slow-release fertilizer and preparation method thereof |
| CN1634808A (en) * | 2003-12-26 | 2005-07-06 | 上海化工研究院 | Manufacturing method of sulfur-coated slow-release chemical fertilizer |
| CN1569774A (en) * | 2004-04-27 | 2005-01-26 | 山东农业大学 | Heavy polymer coated slow-release fertilizer with sulfide as bottom coat |
| CN1609063A (en) * | 2004-08-11 | 2005-04-27 | 吴成祥 | Slowly controlled releasing sulfur-containing urea and its prepn process |
| CN1657512A (en) * | 2005-02-05 | 2005-08-24 | 方连明 | Release controlled coated fertilizer and its composition and preparation method |
Cited By (27)
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|---|---|---|---|---|
| US8741021B2 (en) | 2008-07-16 | 2014-06-03 | Agrium Inc. | Controlled release fertilizer composition |
| US8741022B2 (en) | 2008-07-16 | 2014-06-03 | Agrium Inc. | Controlled release fertilizer composition |
| EP2310344A4 (en) * | 2008-07-16 | 2015-03-11 | Agrium Inc | Controlled release fertilizer composition |
| US7771505B2 (en) * | 2008-07-16 | 2010-08-10 | Agrium Inc. | Controlled release fertilizer composition |
| WO2012025899A1 (en) | 2010-08-26 | 2012-03-01 | Dominó - Indústrias Cerâmicas Sa | Fragrance slow-release silica-based layer, ceramic tile and production process thereof |
| WO2012138210A1 (en) * | 2011-04-05 | 2012-10-11 | Universiti Teknologi Petronas | Multilayer controlled release fertilizer and method for producing the same |
| EP4474370A3 (en) * | 2014-05-05 | 2025-02-19 | SABIC Global Technologies B.V. | Coated granular fertilizers, methods of manufacture thereof, and uses |
| US11401218B2 (en) | 2014-05-05 | 2022-08-02 | Sabic Global Technologies B.V. | Coated granular fertilizers, methods of manufacture thereof, and uses |
| EP3693351A3 (en) * | 2014-05-05 | 2020-12-09 | SABIC Global Technologies B.V. | Coated granular fertilizers, methods of manufacture thereof, and uses |
| US11104618B2 (en) | 2015-07-20 | 2021-08-31 | Sabic Global Technologies B.V. | Fertilizer composition and methods of making and using same |
| US11124463B2 (en) | 2015-11-16 | 2021-09-21 | Sabic Global Technologies B.V. | Coated granular fertilizers, methods of manufacture thereof, and uses thereof |
| US12234197B1 (en) | 2015-11-16 | 2025-02-25 | SABIC Agri-Nutrients Company | Coated granular fertilizers, methods of manufacture thereof, and uses thereof |
| US11806689B2 (en) | 2016-02-08 | 2023-11-07 | Sabic Global Technologies B.V. | Method of making a fertilizer seed core |
| US11802097B2 (en) | 2017-04-19 | 2023-10-31 | Sabic Global Technologies B.V. | Enhanced efficiency fertilizer with urease inhibitor and nitrification separated within the same particle |
| US12006273B2 (en) | 2017-04-19 | 2024-06-11 | SABIC Agri-Nutrients Company | Enhanced efficiency fertilizer with urease inhibitor and nitrification inhibitor in separate particles |
| US11306037B2 (en) | 2017-04-19 | 2022-04-19 | Sabic Global Technologies B.V. | Enhanced efficiency fertilizer with urease inhibitor and nitrification separated within the same particle |
| US11358908B2 (en) | 2017-04-19 | 2022-06-14 | Sabic Global Technologies B.V. | Enhanced efficiency fertilizer with urease inhibitor and nitrification inhibitor in separate particles |
| US20220251002A1 (en) * | 2017-04-19 | 2022-08-11 | Sabic Global Technologies B.V. | Enhanced efficiency fertilizer with urease inhibitor and nitrification inhibitor in separate particles |
| US11345645B2 (en) | 2017-04-20 | 2022-05-31 | Sabic Global Technologies B.V. | Enhanced efficiency fertilizer with embedded powder composition |
| US11021409B2 (en) | 2017-08-09 | 2021-06-01 | Sabic Global Technologies B.V. | Extruded fertilizer granules with urease and/or nitrification inhibitors |
| CN109265249A (en) * | 2018-10-31 | 2019-01-25 | 湖北富邦科技股份有限公司 | Delay the method for molten fertilizer for delaying the activator of molten object and using activator preparation |
| CN110981602A (en) * | 2019-12-17 | 2020-04-10 | 中盐安徽红四方肥业股份有限公司 | Coated slow-release fertilizer for rice and preparation method and application thereof |
| CN113717010A (en) * | 2021-09-07 | 2021-11-30 | 新洋丰农业科技股份有限公司 | Preparation method of zinc efficient corn special fertilizer suitable for calcareous soil |
| CN114163284A (en) * | 2022-01-21 | 2022-03-11 | 黑龙江省昊千生物科技有限公司 | Flushing compound fertilizer uniformly applied by oil dispersion and production processing device thereof |
| CN115926347A (en) * | 2022-11-18 | 2023-04-07 | 河北工业大学 | Biodegradable mulching film for slow release of fertilizer and preparation method and application thereof |
| CN117859593A (en) * | 2024-03-12 | 2024-04-12 | 云南省农业科学院农业环境资源研究所 | Planting method for preventing and controlling bacterial wilt of continuous cropping tomatoes by using carbon-based biofertilizer |
| CN117859593B (en) * | 2024-03-12 | 2024-05-03 | 云南省农业科学院农业环境资源研究所 | A planting method for preventing and controlling bacterial wilt of continuously planted tomatoes using carbon-based biofertilizer |
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