WO2007013219A1 - Iron supplying agent for plant for use in alkaline soil, and process for production of the same - Google Patents
Iron supplying agent for plant for use in alkaline soil, and process for production of the same Download PDFInfo
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- WO2007013219A1 WO2007013219A1 PCT/JP2006/310702 JP2006310702W WO2007013219A1 WO 2007013219 A1 WO2007013219 A1 WO 2007013219A1 JP 2006310702 W JP2006310702 W JP 2006310702W WO 2007013219 A1 WO2007013219 A1 WO 2007013219A1
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- iron
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- alkaline soil
- feo
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- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05D—INORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C; FERTILISERS PRODUCING CARBON DIOXIDE
- C05D9/00—Other inorganic fertilisers
- C05D9/02—Other inorganic fertilisers containing trace elements
Definitions
- the present invention relates to a plant iron supply agent for alkaline soil and a method for producing the same. More specifically, the present invention relates to an iron supplier for plant for alkaline soil having a high Fe 2+ ion concentration in an aqueous solution state and suppressing the acidity of Fe 2+ ions, and a method for producing the same.
- Iron is a trace essential element for plants, and deficiency is known to cause peculiar symptoms such as yellowing of leaves and impaired protein synthesis reaction. In addition, iron is taken in a state of being turned on.
- Fe 3+ ions are known to be difficult to obtain a satisfactory effect on plants even if they are supplied. Therefore, conventionally, it devised to supply iron as Fe 2+ ions have been made.
- Fe 2+ ions is desired to be able to supply an easy tool Fe 2+ ions by prolonged connexion stability becomes Fe 3+ is Sani ⁇ .
- Patent Document 1 As a composition for supplying iron to this plant, the use of iron powder, converter slag, iron hydroxide, etc. has been proposed (for example, see Patent Document 1).
- a method using an inorganic inorganic iron salt a method using an EDTA iron complex with ethylenediamine tetraacetic acid (hereinafter simply referred to as “EDTA”), and the like.
- EDTA ethylenediamine tetraacetic acid
- Patent Document 1 Japanese Patent Laid-Open No. 8-277183
- EDTA is virtually trivalent iron that is used as the EDTA iron complex.
- EDTA is a strong chelating agent, and it is feared that fixing heavy metals in the soil will cause soil contamination, and that it will dissolve into groundwater and cause water contamination.
- the present invention is intended to solve the aforementioned conventional problems, it has a high Fe 2+ I O emissions concentration in aqueous solution, and Fe 2+ for alkaline soils acid I spoon is suppressed ion
- An object is to provide a plant iron supplier (hereinafter sometimes referred to as “plant iron supplier”) and a method for producing the same.
- the present invention is as follows.
- a plant iron supply agent for alkaline soil comprising an aqueous solution obtained by dissolving ascorbic acid and an iron component.
- the iron component is FeO, when containing the Fe 2+ ions and Fe 3+ ions, and the total of the Fe 2+ ions and the Fe 3+ ions is 100 mass%, the Fe The iron supply agent for plant for alkaline soil according to the above (1), wherein the 2+ ion is 50 to 99% by mass.
- the iron component is FeO, a Fe 2+ ion concentration of the aqueous solution, the hydrogen ion exponent measured at 7.0 above area, then the aqueous solution was allowed to stand for 120 hours, again Fe 2+
- the above-mentioned iron component is FeO
- the aqueous solution obtained by dissolving the plant iron supply agent for alkaline soil contains Fe 2+ ions and Fe 3+ ions, and the Fe 2+ ions and the Fe
- the Fe 2+ ion concentration of an aqueous solution in which the iron component is FeO and in which the iron supply agent for alkaline soil plant is dissolved is measured in the region where the hydrogen ion index is 7.0 or more, and then When the aqueous solution is allowed to stand for 120 hours and the Fe 2+ ion concentration is measured again, the concentration after standing is 80% or more of the concentration before standing, for alkaline soil according to (8) above Plant iron supply.
- An iron supply agent for plants for alkaline soil characterized by comprising a granular material containing ascorbic acid and an iron component in a matrix made of peat and / or clay.
- a heating step comprising heating a mixture containing ascorbic acid powder, iron component powder, and water to provide an aqueous solution obtained by dissolving the ascorbic acid powder and the iron component powder.
- the above FeO powder is prepared by vacuum heating a granulated product obtained by granulating iron-containing dust and a granulated product obtained by granulating Z or iron-containing dust and a reducing agent.
- a method for producing an iron supply agent for a plant for alkaline soil characterized by granulating.
- the above FeO powder is prepared by vacuum heating a granulated product obtained by granulating iron-containing dust and a granulated product obtained by granulating Z or iron-containing dust and a reducing agent.
- An aqueous solution obtained by dissolving ascorbic acid and an iron component, and an aqueous solution obtained by dissolving ascorbic acid and an iron component According to another iron supply agent for alkaline soil plants of the present invention obtained by removing Particularly when the iron component is FeO, obtained higher Fe 2+ ion concentration. That is, for example, even when water is dissolved in soil, a high Fe 2+ ion concentration can be obtained, and iron can be supplied with high probability. Further, the resulting Fe 2+ ions for effectively Sani spoon is suppressed, it is the supply of iron at a high probability. In addition, because it uses ascorbic acid, it is safe to use with no environmental impact.
- iron component is FeO and has a predetermined Fe 2+ ion ratio
- iron can be supplied with a particularly high probability.
- the iron component is FeO and the pH is measured in the region of 7.0 or more, and then the Fe 2+ ion concentration after standing for a predetermined time is 80% or more immediately after the start of measurement, it is particularly high. It has antioxidant properties and can supply Fe 2+ ions stably over the long term.
- a biodegradable binder when contained, it can be set as the iron supply agent for plants which has the sustained release property which supplies Fe ⁇ 2+ > stably and gradually over a long period of time.
- the Fe 2+ supply amount can be easily kept within an appropriate range, and the versatility is excellent.
- the iron component for alkaline soil according to the present invention comprises a granular material in which ascorbic acid and an iron component are contained in a matrix made of peat and / or clay.
- a plant iron supply agent having a sustained release property that supplies Fe 2+ particularly stably and gradually can be obtained.
- ascorbic acid and FeO contained as an iron component 100% by mass
- ascorbic acid is 1 to 30% by mass
- FeO is 1 to 30% by mass. In this case, it is possible to obtain an iron supply agent for plants having more reliable sustained release.
- the plant iron supply agent for alkaline soil according to the present invention comprising the aqueous solution obtained by dissolving ascorbic acid and the iron component is stabilized. Can be obtained reliably.
- the aqueous solution when the aqueous solution is equipped with a drying process for removing water, the aqueous solution obtained by dissolving ascorbic acid and the iron component is used to remove water from the aqueous solution for alkaline soil plants of the present invention.
- An iron supply agent can be obtained stably and reliably.
- still another production method of the present invention including a granulation step, it is possible to stably and reliably obtain an iron supply agent for alkaline soil plants having a sustained release property using peat and / or clay as a matrix. it can.
- the ascorbic acid powder is 1-30% by mass
- the FeO powder power is 30% by mass. It can be used as an agent.
- the iron component powder is FeO powder
- this FeO powder is vacuum-quenched after the granulated product is heated in vacuum.
- the FeO powder obtained in this way it is possible to reliably and stably obtain a plant iron supply agent that has particularly high acidity and contains FeO.
- FIG. 3 is an explanatory diagram showing a comparison of the growth situation of the above-ground part of Experimental Example 8 using only fertilizer and the growth situation of the above-ground part of rice of Experimental Examples 9 and 10.
- FIG. 4 is an explanatory diagram showing a comparison of the growth situation of the above-ground part of Experimental Example 8 using only fertilizer and the growth situation of the upper part of the rice of Experimental Examples 11 and 12.
- FIG. 5 is an explanatory view showing a comparison of the growth situation of the above-ground part of Experimental Example 8 using only fertilizer and the growth situation of the upper part of the rice of Experimental Examples 13 and 14.
- FIG. 6 is an explanatory diagram showing a comparison of the growth situation of the above-ground part of Experimental Example 8 using only fertilizer and the growth situation of the upper part of the rice of Experimental Examples 15 and 16.
- FIG. 8 is an explanatory diagram showing a comparison of the growth situation of the above-ground part in Experimental Example 8 using only fertilizer and the growth situation of the root part of rice in Experimental Examples 9 and 10.
- FIG. 9 is an explanatory diagram showing a comparison of the growth situation of the above-ground part in Experimental Example 8 using only fertilizer and the growth situation of the root part of rice in Experimental Examples 11 and 12.
- FIG. 10 is an explanatory diagram showing a comparison of the growth situation of the above-ground part in Experimental Example 8 using only fertilizer and the growth situation of the root part of rice in Experimental Examples 13 and 14.
- FIG. 11 is an explanatory diagram showing a comparison of the growth situation of the above-ground part in Experimental Example 8 using only fertilizer and the growth situation of the root part of rice in Experimental Examples 15 and 16.
- the plant iron supply agent for alkaline soil according to the present invention (hereinafter simply “the iron supply agent for plants” t t) is composed of an aqueous solution obtained by dissolving ascorbic acid and an iron component.
- Another plant iron supplier for alkaline soil of the present invention (hereinafter simply referred to as “the other plant iron supplier”) has an aqueous solution obtained by dissolving ascorbic acid and an iron component. It is characterized by removing. That is, the other iron supply agent for plants can be obtained by removing water from the iron supply agent for plants.
- Still another plant iron supply agent for alkaline soil according to the present invention contains peat and / or a matrix that also has clay power, ascorbic acid and an iron component. It consists of the contained granular material, It is characterized by the above-mentioned.
- Alkaline soil in each of the above inventions means that when 10g of air-dried soil is charged with 25ml of distilled water and shaken for 1 hour and the pH of the resulting suspension is measured, the pH is 7 This refers to soil that exceeds the threshold.
- the alkaline soil includes alkaline soil obtained by alkaline conversion of the original alkaline soil and non-alkali soil, for example, by fertilization, desert rehabilitation, or the like.
- Examples of the above basic alkaline soil include soils containing various calcareous components such as shell fossil soil, calcareous soil, and clay soil. These may be used alone or in combination of two or more. In addition, these various calcareous components It is a mixed soil of potash soil and non-alkaline soil, and it is included after being alkaline soil as a whole.
- the “iron component” in each of the above inventions is not particularly limited, and may be metallic iron such as iron powder, which may be an iron compound.
- the iron compound is not particularly limited, but a compound having divalent iron in the molecule is more preferable.
- the iron compound include oxides such as FeO, FeSO, Fe
- inorganic salts such as FeCl
- organic salts such as trimethoxy iron and Fe-EDTA, Fe-ED
- iron component is metallic iron and Z or FeO, preferably S, more preferably FeO.
- the “ascorbic acid” is an organic acid having a hydroxyl group. This ascorbic acid has no irritating odor. When an aqueous solution containing ascorbic acid and an iron component is prepared, the Fe 2+ ion concentration relative to the ascorbic acid concentration can be increased.
- the "aqueous solution” is an aqueous solution obtained by dissolving ascorbic acid and an iron component.
- this aqueous solution is an aqueous solution that does not contain easily dissolved ascorbic acid and not easily dissolved pig iron component.
- this aqueous solution may be a supernatant in a solid-liquid coexisting material containing ascorbic acid and / or an iron component that cannot be dissolved.
- the dissolved state of ascorbic acid and the iron component in the aqueous solution is not particularly limited. That is, for example, the aqueous solution of ascorbate and ascorbate ions can be contained in this aqueous solution. Among these, it is particularly preferred that an iron ascorbate complex is contained.
- the amount of ascorbic acid dissolved in this aqueous solution is not particularly limited. Usually, the amount of ascorbic acid per 100 ml of water is 0.05 g or more (preferably 0.5 g to the solubility of ascorbic acid at the temperature of the aqueous solution). is there. On the other hand, the iron component can be added in an amount of 10 to 25 parts by mass, particularly 20 to 25 parts by mass, with ascorbic acid being 100 parts by mass.
- the water constituting the aqueous solution is not particularly limited, and various types of water can be used. Tap water and industrial water that can be highly purified water such as pure water and ion exchange water Ordinarily used water such as agricultural water and groundwater may be used.
- the method for obtaining this aqueous solution is not particularly limited, but can be obtained by a production method described later. That is, it can be obtained by heating a mixture containing (1) ascorbic acid powder, iron component powder, and water. In addition, (2) it can also be obtained by adding an iron component powder to an ascorbic acid aqueous solution in which the entire amount is dissolved in advance and heating. Alternatively, (3) an ascorbic acid powder and an iron component powder may be further added to an ascorbic acid aqueous solution in which a predetermined amount is dissolved in advance and heated. Furthermore, (4) it can be obtained by mixing ascorbic acid powder, iron component powder and water without heating. Further, (5) in addition to the above (1) to (4), when dissolved, lascosulvic acid and dissolved, and when FeO is contained, these are separated by a method such as filtration. It can be set as the manufacturing method provided with a process.
- the plant iron supply agent may contain a pyroligneous acid solution for fungicide.
- the content of the wood vinegar is preferably 10% by mass or less (usually 5% by mass or more) of the whole iron supply agent for plants.
- ultraviolet irradiation can be performed in advance for the same purpose.
- the ultraviolet irradiation conditions are not particularly limited, it is preferable to use ultraviolet rays having a wavelength of 200 to 380 nm.
- irradiation it is preferable to irradiate 72 ⁇ 10 w ′s / cm 2 or more.
- the temperature is not particularly limited! / ⁇ is preferably 15 ° C or less.
- This other iron supply agent for plants is obtained by removing the aqueous solution water.
- the above “removal” means an operation of removing a part or all of water from the aqueous solution, but usually the water content with respect to the whole other iron supply agent for plants is 90% by mass or less.
- the water content is 10% by mass or less (preferably 5% by mass or less) for solid materials, and the water content is 60 to 90% by mass (preferably 65 to 85% by mass) for pastes.
- the other iron supply agent for plants may be a solid material from which substantially all water has been removed from the aqueous solution, or may be a paste-like material from which some water has been removed from the aqueous solution. Of these, solids are preferred.
- the method for removing the water is not particularly limited, and drying under reduced pressure, drying under normal pressure, Means such as thermal vacuum drying and freeze-drying can be used. Of these, vacuum drying is preferred. This is because it is possible to suppress the oxidation of Fe 2+ during the process of removing water. In addition to drying under reduced pressure, drying under a low oxygen partial pressure may be used.
- the temperature of the aqueous solution is not particularly limited, but is preferably maintained at 120 ° C or lower. When the temperature exceeds 120 ° C, the Fe 3+ ion concentration tends to increase.
- the temperature of the aqueous solution by this heating is particularly preferably 100 ° C. or less, more preferably 90 ° C. or less, and further preferably 70 ° C. or less.
- the lower limit temperature is not particularly limited, and may be any temperature that causes transpiration of water under the pressure when removing water.
- the temperature of the aqueous solution is, for example, preferably 45 ° C or higher, more preferably 50 ° C or higher, more preferably 55 ° C or higher, particularly preferably 60 ° C or higher, and particularly preferably 65 ° C or higher. .
- These upper limit temperature and lower limit temperature in the heating can be combined. That is, for example, 45 to 120 ° C is preferable, 50 to 100 ° C is more preferable, and 60 to 70 ° C is more preferable. Combinations other than these may be used.
- the pressure is not particularly limited, but is preferably 0.1 to 50 kPa force S, more preferably 0.1 to 20 kPa force S, more preferably 3 to 15 kPa force, 4 to 1 OkPa is particularly preferred.
- the other iron supply agents for plants can be dissolved almost entirely in water having a temperature of 15 ° C or higher.
- the properties of the aqueous solution in which this other iron supply agent for plants is dissolved will be described later.
- the method of using the other iron supply agent for plants is not particularly limited.
- it can be mixed with soil (powdered or lump), sprayed on soil (powdered), or buried in soil (powdered or lump).
- the Fe 3+ ion concentration is dissolved by stirring and mixing in ion-exchanged water at a temperature of 20 ° C so that the concentration of the iron supply agent is 10 gZ liter (about 1.0% by mass) (stir for about 5 minutes). Then, filter using a membrane filter (pore size 1 ⁇ m). Immediately after filtration, attach a water quality measurement pack to an ultraviolet / visible light spectrophotometer (Shimadzu Corporation, model “UV1240”). The amount of Fe 2+ ions and the total amount of Fe ions contained in the aqueous solution were measured, and the total amount of Fe ions was also calculated by subtracting the amount of Fe 2+ ions.
- the plant iron supply agent and the other plant iron supply agents may contain a biodegradable binder.
- a biodegradable binder By containing a biodegradable binder, the iron supply is gradually released as the binder is decomposed to produce Fe 2+ . Therefore, it is possible to supply Fe 2+ ions stably over a long period of time. That is, sustained release can be imparted to the plant iron supply agent and the other plant iron supply agents.
- Biodegradable plastic As the biodegradable binder, a biodegradable plastic can be used.
- Biodegradable plastics include polybutylene succinate-based resin, polylactic acid-based resin, urea resin, poly-strength prolatatone-based resin, cellulose-based resin, starch-based resin, and polybut alcohol. And the like. These may be used alone or in combination of two or more.
- the content of the biodegradable binder is not particularly limited. However, when the total amount of the iron supply agent for plants and the other iron supply agent for plants is 100% by mass, 10% by mass or less (more preferably 2 to 7% by mass, usually 1% by mass or more).
- the plant iron supply agent and the other plant iron supply agents may contain a biodegradable extender.
- the biodegradable extender is a component other than the above binder having biodegradability. Examples of this biodegradable bulking agent include rice husk, snow flora, rice bran, shochu, sake lees, taenic acid lees, straw, peat, humus, chicken manure, compost, cow manure and bone meal. These may be used alone or in combination of two or more.
- the biodegradable extender may or may not have a predetermined function for plants. Examples of the component having a predetermined function include components that serve as nutrients for plants.
- the content of the biodegradable extender is not particularly limited, but it is 50 to 94% by weight (preferably 70% when the total amount of the iron supply agent for plants and other iron supply agents for plants is 100% by weight). ⁇ 94 mass%). Within this range, an appropriate amount can be mixed even when a small amount of plant iron supplier is mixed with a large amount of soil.
- the plant iron supply agent and the other plant iron supply agents may contain other components in addition to the biodegradable binder and the biodegradable extender.
- Other components include lipoic acid, oryza oil, various vitamins, Mn, Zn, Cu, Cr, Si, Mg, Ca, Co, Mo, Ni, B, etc. (for example, metallic state, metallic Acid compounds), and compounds such as S and C1. These may be used alone or in combination of two or more.
- the other ingredients are 10 parts by mass or less when the total of the biodegradable binder and biodegradable extender contained in the plant iron supplier and other plant iron supplier is 100 parts by mass. It is preferable that
- the method for using the plant iron supply agent and the other plant iron supply agents is not particularly limited.
- peat and Z or clay are contained in the other iron supply agents for plants using a biodegradable extender as a matrix.
- biodegradable extenders are water-repellent, and when this other plant iron supply is used in alkaline soil, it can be used as an aqueous solution with a high pH from the surroundings. As the pH is kept low, the decrease in solubility of FeO is suppressed, and the acidity of Fe 2+ ions is further suppressed. Therefore, Ru can be supplied to prolonged connexion stable Fe 2+ ions. That is, excellent sustained release properties can be imparted by the present other iron supply agent for plants.
- this other iron supply agent for plants includes a biodegradable extender having water repellency, peat and Z, or a granule containing ascorbic acid and an iron component in a matrix having clay power.
- a biodegradable extender having water repellency, peat and Z or a granule containing ascorbic acid and an iron component in a matrix having clay power.
- the shape of the particles constituting the granular body is not particularly limited, and may be any of a sphere, an ellipsoid, a hemisphere, a cube, a cuboid, a cylinder, a plecket, and the like.
- the granular body may be a dense body or a porous body.
- the particle size (diameter in the case of a sphere, maximum interstitial dimension in the case of other shapes) is preferably 50 mm or less (more preferably 10 mm or less, further preferably 6 mm or less, usually 0.5 mm or more).
- ascorbic acid contained as an iron component, and peat and / or clay as biodegradable extenders.
- total 100% by weight
- Asukorubin acid is contained 1 to 30 wt%
- FeO is preferably are contained 1-30 wt 0/0.
- the content of this ascorbic acid is more preferably 3 to 20% by mass, particularly preferably 7 to 13% by mass.
- the content of FeO is more preferably 3 to 20% by mass, particularly preferably 7 to 8% by mass. .
- the water-repellent biodegradable extender suppresses the contact of iron components such as ascorbic acid and FeO with the external environment, thereby further reducing other plant iron supply agents.
- iron components such as ascorbic acid and FeO
- the increase in pH inside the granular material is suppressed. This suppresses the decrease in the solubility of FeO.
- the acid of ascorbic acid due to oxygen in the air As a result, the effect of ascorbic acid on the suppression of the acid content of iron components such as FeO can be obtained, and Fe 2+ ions can be supplied more stably over a long period of time.
- this other iron supply agent for plants using a biodegradable extender as a matrix.
- it can be mixed with the soil (in powder form or in a lump form), sprayed on the soil (in powder form), or embedded in the soil (in powder form or lump form).
- the production method of the present invention is not particularly limited as described above, and various methods can be used. For example, by heating a mixture containing ascorbic acid powder, iron component powder, and water, A dissolution step for obtaining an aqueous solution obtained by dissolving ascorbic acid and an iron component can be provided.
- the "ascorbic acid powder” is a powder containing ascorbic acid as a main component (usually having a purity of 99% or more), and the purity is not particularly limited. Moreover, when it is a powder form, the particle shape etc. are not specifically limited.
- the “iron component powder” is a powder mainly composed of the various iron components. This iron component powder is preferably FeO powder.
- the amount of FeO contained in the FeO powder is not particularly limited, but usually FeO is 50 mass% or more (preferably 65 mass% or more, preferably 100 mass% or more based on the entire FeO powder). It may be mass%).
- This FeO powder can be any type of FeO powder.
- the FeO powder described later (a granulated product obtained by granulating iron-containing dust (hereinafter sometimes referred to as “dust”), and Z or A granulated product obtained by granulating this dust and a reducing agent, FeO powder obtained by vacuum heating and vacuum quenching), and various commercially available FeO powders can be used.
- dust a granulated product obtained by granulating iron-containing dust
- various commercially available FeO powders can be used.
- FeO powder obtained by heating the granulated product in a vacuum and then quenching in a vacuum is preferable.
- any water can be used as described above.
- the amount of ascorbic acid powder and iron component powder such as FeO powder and water charged in the above “mixture” is not particularly limited, but ascorbic acid powder (assuming purity 100%): iron component powder (purity 100 (Assuming%): The mass ratio of water (assuming purity of 100%) is preferably 60-90: 7-28: 3-20, 65-85: 10-24: 5-17 Use at a rate of 5 It is particularly preferable to use it at a ratio of 68-72: 10-22: 10-15.
- the above mixture may or may not contain other components besides ascorbic acid powder, iron component powder and water.
- other components When other components are contained, they may be contained in a state dissolved in water or in a state not dissolved in water.
- examples of other components include methanol and ethanol. By containing these, water can be removed more smoothly even under a reduced pressure environment. These may contain only one kind or two or more kinds.
- the heating conditions in the above "heating” are not particularly limited, but the heating temperature is preferably maintained at 120 ° C or lower. This is because the Fe 3+ ion concentration tends to increase above 120 ° C.
- the temperature of the aqueous solution by this heating is more preferably 110 ° C. or less, more preferably 105 ° C. or less, and further preferably 100 ° C. or less.
- the lower limit temperature is not particularly limited.
- 40 ° C or higher is preferable, 50 ° C or higher is more preferable, and 60 ° C or higher is particularly preferable.
- the upper limit temperature and the lower limit temperature at the time of heating can be combined. That is, for example, 40 to 120 ° C is preferable, and 50 to 110 ° C is more preferable, and 60 to 100 ° C is more preferable. Combinations other than these may be used.
- the pressure conditions for heating are not particularly limited.
- This heating is dissolved in more water Asukorubin acid, which in accordance with the amount of dissolved TetsuNaru components such as FeO even more, even Noto consider the concentration of Fe 2+ ions or Fe 2+ ion complex of interest is higher It is done.
- the production method of the present invention can include a step of removing the water-insoluble component after the dissolution step.
- the water-insoluble component include ascorbic acid powder that cannot be dissolved and iron component powder that cannot be dissolved.
- the removal method is not particularly limited, but can usually be performed by filtration. That is, a filtration step can be provided.
- the filtration conditions at this time are not particularly limited. For example, it is preferable to use a membrane filter having a pore size of 10 m or less (more preferably 5 ⁇ m or less, more preferably 3 ⁇ m or less) as the filtration filter.
- a drying step for removing water from the aqueous solution is further provided after the dissolution step or after the dissolution step and the filtration step.
- the drying conditions in this drying step are not particularly limited, and natural drying may be performed, but it is preferable to use the above-described removal method and drying conditions. That is, it is preferable to remove water by heating under reduced pressure. By heating and gradually reducing the water content, Fe 2+ ion components (Fe 2+ complex, etc.) that are water-soluble and have excellent acid-fast properties are concentrated, and other plant iron suppliers Is considered to be obtained.
- a purification step is a process for purifying water-soluble components. That is, for example, extraction is performed by removing the water-insoluble components in the same manner as described above after contacting the iron supply agent for plants obtained by removing water from the aqueous solution with water to dissolve the soluble portion. A step and a re-drying step for removing water from the extraction aqueous solution obtained in this extraction step.
- biodegradable extenders having water repellency (usually powder or granules).
- water repellency usually powder or granules.
- Peat and Z or clay, ascorbic acid powder, and iron component powder are mixed and granulated.
- the mixing method is not particularly limited, and it may be mixed by a dry kneader using a mortar mixer, an omni mixer or the like, or a kneader or a wet pan.
- the granulation method is not particularly limited, but it is usually granulated by an extrusion method. Further, it is preferable that mixing and granulation are continuously performed by extrusion molding because the process can be simplified.
- the temperature of the dry blending and extrusion molding is not particularly limited, and it may be room temperature (for example, 15 to 35 ° C) or may be heated to about 40 to 90 ° C if necessary! /.
- iron supply agent for plants of this invention is applicable as it is.
- the total of FeO powder blended as peat and / or clay, ascorbic acid powder and iron component powder is 100 mass%, ascorbic acid powder is 1-30 mass%, FeO powder is 1-30 mass%. It is blended in mass%.
- Still other plant iron supplies include peat and Z or clay and the other plant iron supplies. It can also be obtained by mixing with a feed agent and granulating. The mixing and granulation at this time can be performed in the same manner as described above.
- the mass proportions of peat and / or clay, ascorbic acid powder, and FeO powder are the same as above, and this mass proportion is the same as that of other plants. It can be adjusted according to the mass ratio of ascorbic acid powder and FeO powder used in the production of iron supplements and the mass ratio of peat and / or clay and other iron supplements for plants. .
- this FeO powder is a granulated product obtained by granulating dust containing iron, and Z Or, it is preferable to use a FeO powder obtained by vacuum-cooling a granulated product obtained by granulating this dust and a reducing agent.
- this FeO powder is usually CaAl O, FeAl O, CaFe Si O, CaSi.
- the content of the double oxide is preferably 0.5 to 10% by mass when the entire FeO powder is 100% by mass. Within this range, it is possible to obtain an iron supplier that is particularly excellent in acid resistance.
- the particle diameter of the particles constituting the FeO powder is not particularly limited, but may be any FeO powder having a particle diameter force of 000 ⁇ m or less and a mixture of powders having various particle diameters. Furthermore, porous particles may be included.
- the "dust containing iron” is one containing iron (dust collection powder or the like).
- the iron component include iron oxide, other iron compounds, and metallic iron. These may contain only one kind or two or more kinds.
- the amount of iron contained in the dust is not particularly limited, but usually 30% by mass or more (more preferably 35 to 90% by mass, still more preferably 40 to 80% in terms of metallic iron when the total dust is 100% by mass. Mass%).
- the dust may contain other components besides iron.
- Other components include Zn, Ni, Cu and Mn. These may be simple metals or compounds such as oxides. Furthermore, these may contain only 1 type, and may contain 2 or more types.
- the shape of the dust containing iron is not particularly limited, and may be small pieces or a mixture of powder and small pieces, but is usually powder.
- the average particle size of this powder is not particularly limited
- Examples of the dust containing iron include forged shot dust collected in the forging process and steelmaking dust such as electric furnace dust, blast furnace dust, converter dust, and cupola dust generated in the steel making process. These may be used alone or in combination of two or more.
- dust from which the chlorine content has been removed by washing with water (partially or entirely) is preferred.
- the chlorine content in the dust is preferably 0.5% by mass or less (more preferably 0.4% by mass or less, and still more preferably 0.3% by mass or less).
- the above "granulated product” contains iron-containing dust or the dust and a reducing agent. Granulation reduces or converts Fe O, Fe 2 O and Fe (single) to FeO or acid during vacuum heating
- the shape of the particles constituting the granulated product is not particularly limited, and may be any of a sphere, an ellipsoid, a hemisphere, a cube, a cuboid, a cylinder, a plecket, and the like. Further, the granulated product may be a dense body or a porous body. Further, the particle size (diameter in the case of a sphere, shortest dimension in the case of other shapes) is preferably 25 mm or less (more preferably 15 mm or less, further preferably 10 mm or less, usually 3 mm or more).
- the "reducing agent” is a component that reduces an iron compound that has been oxidized to a valence of 2 or more.
- metallic iron, a mixture thereof, carbon, a mixture thereof, or the like can be used.
- reducing agents used for iron cutting scraps, iron polishing scraps, iron powder, pig iron and steel, various waste materials (tire scraps, wood waste materials, etc.) and the like are preferable. These may be used alone or in combination of two or more.
- the shape of the reducing agent is not particularly limited, but it is preferable that the contact area with the dust is large, so that powder, granules, small pieces, etc. are particularly preferable. Furthermore, the average particle size is preferably 200 m or less (preferably 180 ⁇ m or less).
- the content of the reducing agent in the granulated product is not particularly limited, but when the dust is 100 parts by mass, it is 100 parts by mass or less (more preferably 90 parts by mass or less, more preferably 80 parts by mass or less, usually 30 parts by mass). More than part).
- the granulated product usually contains noinda.
- the type of binder is not particularly limited, but alumina cement is preferable.
- the blending amount is 3 to 20 parts by mass (more preferably 3 to 15 parts by mass, further preferably 3 to 12 parts by mass) when the dust containing iron content or the total of the dust and the reducing agent is 100 parts by mass. Part). In this range, granulation can be performed smoothly and embrittlement of the granulated product can be suppressed.
- the FeO concentration in the FeO powder can be increased.
- the degree of vacuum during this vacuum heating is not particularly limited, but is preferably 0.1 to 13.3 kPa (more preferably 2.6-13. 3 kPa, particularly preferably 4.0 to 6.7 kPa). Within this range, it is possible to effectively suppress residual metallic iron and oxidation of FeO to Fe 2 O and the like. This vacuum atmosphere
- the heating temperature (measured value obtained by measuring the granulated product itself) during vacuum heating is preferably 600 to 1100 ° C (more preferably 800 to 950 ° C). However, when the granulated product contains a reducing agent, it is preferably 800 ° C or higher. In this range, FeO powder having a particularly high FeO content can be obtained, and it is possible to prevent melting of iron-containing dust during the heating process.
- the heating time is not particularly limited, but is preferably 30 minutes or longer (more preferably 30 minutes or longer and within 6 hours).
- the granulated product is usually heated using a heat treatment furnace.
- the heat treatment furnace is not particularly limited as long as it includes at least a heater and can uniformly heat the granulated product to be charged.
- Examples of the heat treatment furnace include a roller hearth furnace and a rotary kiln.
- the granulated product is powdered by, for example, a stirring means equipped with a stirring blade while moving in the heat treatment furnace.
- This heat treatment furnace may be equipped with a recovery device for recovering metallic zinc and the like produced by the reduction.
- the amount of granulated product input to the heat treatment furnace is not particularly limited ⁇ Considering heat conduction to the entire granulated product heated in the 1S heat treatment furnace, the average height of the granulated product sprayed on the hearth is Usually, it is 100mm or less, especially 80mm or less, and 30mm or less. It is preferable that it is an amount.
- the high-temperature FeO powder produced by vacuum heating can be cooled without being oxidized.
- the degree of vacuum during this vacuum quenching is not particularly limited, but is preferably 13.3 kPa or less (more preferably 6.7 kPa or less, usually 5.3 kPa or more).
- the temperature drop rate is not particularly limited, but is preferably 5 to 150 ° CZ. In this vacuum quenching, it is preferable to cool to 300 ° C or lower (more preferably 200 ° C or lower, particularly preferably 150 ° C or lower).
- a granulated product containing metallic iron for the purpose of obtaining FeO powder having a higher FeO content, it is preferable to use a granulated product containing metallic iron.
- the content of metallic iron is preferably 5% by mass or more (more preferably 5 to 85% by mass, still more preferably 8 to 50% by mass) when the total amount of iron contained in the granulated product is 100% by mass.
- this granulated product for example, an FeO powder having a FeO content of 80 mass% or more (more preferably 85 mass% or more, particularly 90 mass% or more) based on the total iron content can be obtained.
- Fe80 mass 0/0 (hereinafter,% abbreviated.), ZnO. 02%, CaO. 01%, MnO. 06% and SiO. 06% or the like is contained, forging shot dust collecting an average particle diameter of 100 m It was granulated into a cylindrical shape having a diameter of 8 mm and a length of about 20 mm using 82% of powder, 10% of iron powder having an average particle diameter of 75 m, 5% of alumina cement, and 3% of bentonite. The obtained granulated product was heated in a vacuum heating tank (roller and hearth furnace) at 800 ° C. for 30 minutes, then at 850 ° C. for 30 minutes, and then at 900 ° C. for 1 hour.
- a vacuum heating tank roll and hearth furnace
- vacuum quenching is performed in a vacuum quenching bath to 400 ° C at a temperature drop rate of 20 ° CZ, and further vacuum
- the atmosphere in the cooling tank was replaced with nitrogen, and further cooled to 200 ° C at a rate of temperature decrease of 13 ° CZ, and then cooled to room temperature to obtain FeO powder.
- FeO contained in this FeO powder was quantified by a calibration curve prepared in advance by X-ray diffraction using a mixed powder obtained by mixing a reagent FeO powder and silicon powder at a predetermined ratio, the content was It was 90% by mass.
- aqueous solution of ascorbic acid was prepared by dissolving 2.5 g of ascorbic acid in 500 ml of distilled water. Thereafter, 1. Og of the FeO powder produced in [1] above was added to this aqueous solution, stirred for 30 minutes, and then filtered to remove impurities. Thereafter, 20 milliliters are taken from the aqueous solution after filtration and put into 5 containers, and ⁇ of the aqueous solution in 4 of these containers is 7.0, respectively, with sodium hydroxide aqueous solution. Adjusted to 8.0 and 9.0. The pH of the ascorbic acid aqueous solution not adjusted for pH was 3.4.
- Example 4 of pH adjustment in 6 1 Each value of pH and Fe ion concentration in the second time is the value at the time of pH adjustment (initial value), and the value of ZpH adjustment power is also a value after 24 hours. In the third pH adjustment, only the initial value was measured.
- Plant iron supply agent for alkaline soil (A) 10% ascorbic acid (purity 99.8% or more), 7.5% FeO powder produced in [1] above, and 82.5% peat processing soil conditioner (trade name, manufactured by Nippon Fertilizer Co., Ltd.) “Kumiai Hyphen” (special name A)) was mixed and granulated by extrusion to produce a roughly spherical spherical iron supply agent (A) for alkaline soil plants.
- Seedling culture soil (b) 100 parts of the fossil shell soil was mixed with 1 part of the fertilizer and 0.1 part of the plant iron supply agent (A).
- Seedling soil (c) 100 parts of the fossil shell soil was mixed with 1 part of the fertilizer and 1 part of the plant iron supply agent (A).
- Fig. 1 is an explanatory diagram based on images obtained by digital photography 10 days after germination of the growth of each seedling in the growth of rice in (A) above ((a), (b) in Fig. 1) And (c) show the results of using the above seedling culture soil (a), (b) and (c), respectively.
- the plant iron supply agent (A) for alkaline soil only fertilizer is blended even though the blending amount is as small as 0.1 part. It can be seen that the seedlings are growing taller than (a).
- the seedlings are particularly taller than (b). You can see that it grows well.
- the plant iron supply agent for alkaline soil (A) produced in [3] and (1) above is opened 1. Pass through an Omm sieve and have a particle size of 1. Omm for plant iron supply for alkaline soil ( B) was obtained.
- Ascorbic acid (purity 99.8%) 800 g and 2 liters of water were put into a stainless steel beaker and stirred at room temperature (20 ° C) to dissolve ascorbic acid in water. Thereafter, 100 g of the FeO powder produced in [1] above was added, and stirring was continued for another 30 minutes. Next, this FeO powder dispersion was filtered using a filter paper, and the filtrate was dried for 72 hours by a drier adjusted to 90 ° C. Thereafter, the obtained paste-like material is cooled to room temperature to form a lump, which is sufficiently pulverized in a mortar, then passed through a sieve with an opening of 1. Omm, and an alkaline soil having a particle size of 1. Omm or less. An iron supply agent for plants (C) was produced.
- the following seedling culture soil was added to each of the cultivation pots, and 20 seeds of rice (variety: Nihonbare) sprouting using a petri dish were directly sown.
- the cocoons were embedded in the soil at a depth of about 0.5 cm from the surface. Then, it was grown using an artificial meteorograph, and the growth promoting action and effect of the above-mentioned plant iron supply agent (A) and the above-mentioned plant iron supply agents (B) and (C) were evaluated.
- the seedlings were grown using an artificial meteorological instrument (manufactured by Nippon Medical Instrumentation, model “LH-100S”).
- the artificial meteorograph was operated with sunshine adjusted to 14 hours (light intensity 1500 lux, temperature 25 ° C) and night time 10 hours (temperature 20 ° C).
- 50 ml of distilled water added to 300 ml of shell fossil soil was used as the field capacity, and irrigated so that the total weight of the pot and contents was maintained at OOg every day throughout the growing period.
- 13 pots throughout the growing period The position was changed randomly every day so that the illumination (sunshine) was evenly irradiated.
- Experimental Example 11 The above fertilizer lg and the above-mentioned fertilizer for plant for alkaline soil (A) l.Og were blended with the fossil shell soil in the pot to prepare a seedling culture soil.
- Experimental Example 12 The above fertilizer lg and the above-mentioned fertilizer for plant for alkaline soil (B) l.Og were blended with the fossil shell soil in the pot to prepare a seedling culture soil.
- Experimental Example 13 The above-mentioned fertilizer lg and the above-mentioned fertilizer for plant for alkaline soil (A) 2. Og were blended with the fossil shell fossil soil in the pot to prepare a seedling culture soil.
- Experimental Example 14 The above-mentioned fertilizer lg and the above-mentioned fertilizer for plant for alkaline soil (B) 2. Og were blended with the fossil shell fossil soil in the pot to prepare a seedling culture soil.
- Experimental Example 16 The above-mentioned fertilizer lg and the above-mentioned fertilizer for plant for alkaline soil (C) l.Og were blended with the fossil shell fossil soil in the pot to prepare a seedling culture soil.
- the seedlings were grown as described above, photographed 54 days after direct seeding of the pods, and harvested. Prior to harvesting, the plant height of 20 seedlings in each pot was measured. Further, the SPAD value (green density, which is an index of the amount of chlorophyll) was measured using a chlorophyll meter (model “SPAD-502” manufactured by Minolta Co., Ltd.). Sift the root soil at harvest, then dry for 7 days, then screen the root soil again to remove almost the entire amount, then take a picture and take the dry weight of the above ground and the dry weight of the root. (Total of dry root weight and weight ) was measured.
- Experimental Examples 9 and 10 except for the SPAD value in Experimental Example 10, the results are better than in Experimental Example 8 in which no plant iron supplier was administered ( Figures 2, 3, and 7). And 8). Further, in Experimental Examples 9 and 10, it is desirable to administer more plant iron supply agents that are not sufficiently promoted in growth compared with Experimental Examples 11 to 14.
- Example 15 Although the SPAD value is low, the plant height, the above-ground dry weight and the root dry weight are sufficient and excellent. This means that in Example 15, the growth of roots is equivalent to Example 16 although the dose is 1Z10 in Example 16. That is, iron should be used preferentially for root growth and then for ground growth. It is guessed how.
- the present invention is not limited to the description of the above-described embodiment, and various modifications can be made within the scope of the present invention.
- a mixture obtained by mixing ascorbic acid powder and iron component powder, adding a small amount of water to the mixture, and then removing the water can be used as an iron supply agent for plants for alkaline soil.
- the amount of water relative to the ascorbic acid powder is not particularly limited, but is usually 5 to 20 parts by mass, more preferably 5 to 15 parts by mass with respect to 100 parts by mass of the ascorbic acid powder.
- the iron component powder can be blended in an amount of 10 to 25 parts by mass, particularly 20 to 25 parts by mass, based on 100 parts by mass of ascorbic acid powder.
- the above ascorbic acid powder and iron component powder the above description can be applied as it is.
- the water content in the solid or paste-like material obtained by using a small amount of water as described above can be set to the same level as the other iron supply agents for plants.
- the water removal method can be the same as that for the other iron supply agents for plants, and drying under reduced pressure is preferable.
- the temperature at the time of heating when removing water and the pressure at which the pressure is reduced when removing water can be the same as those of other iron supply agents for plants.
- the plant iron supply agent for alkaline soil of the present invention is widely used in the field of agriculture and forestry.
- it is widely used for production of agricultural products, hydroponics, production of horticultural plants, maintenance of vegetation in parks and golf courses, maintenance of forests, and the like.
- it is useful as a plant growth promoter in the field of production of various agricultural products.
- it can be used to solve food problems caused by plant growth in barren lands around the world and to improve the global environment by promoting absorption of carbon dioxide.
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Abstract
Description
明 細 書 Specification
アルカリ土壌用植物用鉄供給剤及びその製造方法 Iron supply agent for plant for alkaline soil and method for producing the same
技術分野 Technical field
[0001] 本発明は、アルカリ土壌用植物用鉄供給剤及びその製造方法に関する。更に詳し くは、本発明は、水溶液状態で高い Fe2+イオン濃度を有し、 Fe2+イオンの酸ィ匕が抑 制されたアルカリ土壌用植物用鉄供給剤及びその製造方法に関する。 The present invention relates to a plant iron supply agent for alkaline soil and a method for producing the same. More specifically, the present invention relates to an iron supplier for plant for alkaline soil having a high Fe 2+ ion concentration in an aqueous solution state and suppressing the acidity of Fe 2+ ions, and a method for producing the same.
背景技術 Background art
[0002] 鉄は植物にとって微量必須元素であり、欠乏すると、葉が黄白化する、及び蛋白質 の合成反応が損なわれる等の特有の症状を生じることが知られている。また、鉄はィ オンィ匕された状態で取り込まれる。しかし、 Feイオンのうち、 Fe3+イオンは、これを供 給しても植物に対して満足な効用が得られ難いことが知られている。このため、従来 から、鉄を Fe2+イオンとして供給する工夫がなされている。しかし、 Fe2+イオンは酸ィ匕 されて Fe3+になり易ぐ Fe2+イオンを長期に亘つて安定して供給できることが望まれ ている。 [0002] Iron is a trace essential element for plants, and deficiency is known to cause peculiar symptoms such as yellowing of leaves and impaired protein synthesis reaction. In addition, iron is taken in a state of being turned on. However, among Fe ions, Fe 3+ ions are known to be difficult to obtain a satisfactory effect on plants even if they are supplied. Therefore, conventionally, it devised to supply iron as Fe 2+ ions have been made. However, Fe 2+ ions is desired to be able to supply an easy tool Fe 2+ ions by prolonged connexion stability becomes Fe 3+ is Sani匕.
この植物に対して鉄を供給する組成物として鉄粉や転炉滓、水酸化鉄などの使用 が提案されている (例えば、特許文献 1参照。 ) o更に、硫酸鉄及び硝酸鉄等の水溶 性無機鉄塩を用いる方法、及びエチレンジァミン四酢酸 (以下、単に「EDTA」という )による EDTA鉄錯体を用いる方法等が知られて 、る。 As a composition for supplying iron to this plant, the use of iron powder, converter slag, iron hydroxide, etc. has been proposed (for example, see Patent Document 1). There are known a method using an inorganic inorganic iron salt, a method using an EDTA iron complex with ethylenediamine tetraacetic acid (hereinafter simply referred to as “EDTA”), and the like.
[0003] 特許文献 1 :特開平 8— 277183号公報 Patent Document 1: Japanese Patent Laid-Open No. 8-277183
発明の開示 Disclosure of the invention
発明が解決しょうとする課題 Problems to be solved by the invention
[0004] しかし、特許文献 1に記載の鉄含有組成物から溶出される鉄分は大部分が Fe3+と なり、特にイネ科植物以外の植物が取り込むことは困難であると考えられる。また、上 記水溶性無機鉄塩力も生成する Feイオンは、 Fe2+の状態を保持し難ぐ Fe3+へと酸 化され易い。更に、従来と同様に塩類の蓄積を引き起こすという問題もある。即ち、各 種肥料として水溶性無機金属塩類がこれまで長く使用されており、これら水溶性金属 塩を構成する強酸陰イオンが土壌中の他の元素と結合して水不溶性の塩を形成して 土壌に蓄積することが問題となっている。水溶性無機鉄塩ではこの問題を解消するこ とができない。更に、 EDTA鉄錯体として使用されているのは実質上 3価鉄である。 また、 EDTAは強いキレート化剤であり、土壌中の重金属を固定して土壌汚染を引き 起こすこと、及び地下水に溶け込んで水汚染を引き起こすこと、等が危惧されている [0004] However, most of the iron content eluted from the iron-containing composition described in Patent Document 1 is Fe 3+, and it is considered that it is particularly difficult for plants other than Gramineae plants to take up. In addition, the Fe ions that also generate the water-soluble inorganic iron salt force are easily oxidized to Fe 3+ which is difficult to maintain the Fe 2+ state. Furthermore, there is a problem that salt accumulation is caused as in the conventional case. That is, water-soluble inorganic metal salts have been used for a long time as various fertilizers, and the strong acid anions constituting these water-soluble metal salts combine with other elements in the soil to form water-insoluble salts. Accumulation in soil is a problem. Water-soluble inorganic iron salts cannot solve this problem. Furthermore, it is virtually trivalent iron that is used as the EDTA iron complex. In addition, EDTA is a strong chelating agent, and it is feared that fixing heavy metals in the soil will cause soil contamination, and that it will dissolve into groundwater and cause water contamination.
[0005] 本発明は、上記の従来の問題を解決するものであり、水溶液状態で高い Fe2+ィォ ン濃度を有し、且つ Fe2+イオンの酸ィ匕が抑制されたアルカリ土壌用植物用鉄供給剤 (以下、「植物用鉄供給剤」ということもある。)及びその製造方法を提供することを目 的とする。 [0005] The present invention is intended to solve the aforementioned conventional problems, it has a high Fe 2+ I O emissions concentration in aqueous solution, and Fe 2+ for alkaline soils acid I spoon is suppressed ion An object is to provide a plant iron supplier (hereinafter sometimes referred to as “plant iron supplier”) and a method for producing the same.
課題を解決するための手段 Means for solving the problem
[0006] 本発明は以下のとおりである。 [0006] The present invention is as follows.
(1)ァスコルビン酸と、鉄成分と、が溶解されて得られた水溶液からなることを特徴と するアルカリ土壌用植物用鉄供給剤。 (1) A plant iron supply agent for alkaline soil, comprising an aqueous solution obtained by dissolving ascorbic acid and an iron component.
(2)上記鉄成分が金属鉄及び Z又は FeOである上記(1)に記載のアルカリ土壌用 植物用鉄供給剤。 (2) The plant iron supply agent for alkaline soil according to the above (1), wherein the iron component is metallic iron and Z or FeO.
(3)上記鉄成分が FeOである請求項 2に記載のアルカリ土壌用植物用鉄供給剤。 (3) The plant iron supply agent for alkaline soil according to claim 2, wherein the iron component is FeO.
(4)上記鉄成分が FeOであり、 Fe2+イオンと Fe3+イオンとを含有し、該 Fe2+イオン と該 Fe3+イオンとの合計を 100質量%とした場合に、該 Fe2+イオンが 50〜99質量 %である上記(1)に記載のアルカリ土壌用植物用鉄供給剤。 (4) The iron component is FeO, when containing the Fe 2+ ions and Fe 3+ ions, and the total of the Fe 2+ ions and the Fe 3+ ions is 100 mass%, the Fe The iron supply agent for plant for alkaline soil according to the above (1), wherein the 2+ ion is 50 to 99% by mass.
(5)上記鉄成分が FeOであり、上記水溶液の Fe2+イオン濃度を、水素イオン指数 が 7. 0以上の領域で測定し、その後、該水溶液を 120時間静置し、再び Fe2+イオン 濃度を測定した場合に、静置後の濃度が静置前の濃度の 80%以上である上記(1) に記載のアルカリ土壌用植物用鉄供給剤。 (5) The iron component is FeO, a Fe 2+ ion concentration of the aqueous solution, the hydrogen ion exponent measured at 7.0 above area, then the aqueous solution was allowed to stand for 120 hours, again Fe 2+ The iron supply agent for plant for alkaline soil according to the above (1), wherein the concentration after standing is 80% or more of the concentration before standing when the ion concentration is measured.
(6)生分解性バインダを含有する上記(1)に記載のアルカリ土壌用植物用鉄供給 剤。 (6) The plant iron supply agent for alkaline soil according to (1) above, which contains a biodegradable binder.
(7) 生分解性増量剤を含有する上記(1)に記載のアルカリ土壌用植物用鉄供給 剤。 (7) The plant iron supply agent for alkaline soil according to (1) above, which contains a biodegradable extender.
(8)ァスコルビン酸と、鉄成分と、が溶解されて得られた水溶液力 水を除去してな ることを特徴とするアルカリ土壌植物用鉄供給剤。 (8) Aqueous solution obtained by dissolving ascorbic acid and iron component An iron supply agent for alkaline soil plants.
(9)上記鉄成分が金属鉄及び Z又は FeOである上記(8)に記載のアルカリ土壌用 植物用鉄供給剤。 (9) The plant iron supply agent for alkaline soil according to (8), wherein the iron component is metallic iron and Z or FeO.
(10)上記鉄成分が FeOである上記(9)に記載のアルカリ土壌用植物用鉄供給 剤。 (10) The plant iron supply agent for alkaline soil according to (9), wherein the iron component is FeO.
(11)上記鉄成分が FeOであり、本アルカリ土壌用植物用鉄供給剤を溶解させてな る水溶液は Fe2+イオンと Fe3+イオンとを含有し、該 Fe2+イオンと該 Fe3+イオンとの合 計を 100質量%とした場合に、該 Fe2+イオンが 50〜99質量%である上記(8)に記 載のアルカリ土壌用植物用鉄供給剤。 (11) The above-mentioned iron component is FeO, and the aqueous solution obtained by dissolving the plant iron supply agent for alkaline soil contains Fe 2+ ions and Fe 3+ ions, and the Fe 2+ ions and the Fe The plant iron supply agent for alkaline soil according to (8) above, wherein the Fe 2+ ions are 50 to 99% by mass when the total of 3+ ions is 100% by mass.
(12)上記鉄成分が FeOであり、本アルカリ土壌用植物用鉄供給剤を溶解させてな る水溶液の Fe2+イオン濃度を、水素イオン指数が 7. 0以上の領域で測定し、その後 、該水溶液を 120時間静置し、再び Fe2+イオン濃度を測定した場合に、静置後の濃 度が静置前の濃度の 80%以上である上記(8)に記載のアルカリ土壌用植物用鉄供 給剤。 (12) The Fe 2+ ion concentration of an aqueous solution in which the iron component is FeO and in which the iron supply agent for alkaline soil plant is dissolved is measured in the region where the hydrogen ion index is 7.0 or more, and then When the aqueous solution is allowed to stand for 120 hours and the Fe 2+ ion concentration is measured again, the concentration after standing is 80% or more of the concentration before standing, for alkaline soil according to (8) above Plant iron supply.
(13)生分解性バインダを含有する上記 (8)に記載のアルカリ土壌用植物用鉄供給 剤。 (13) The plant iron supply agent for alkaline soil according to (8), which contains a biodegradable binder.
(14)生分解性増量剤を含有する上記 (8)に記載のアルカリ土壌用植物用鉄供給 剤。 (14) The plant iron supply agent for alkaline soil according to the above (8), which contains a biodegradable extender.
(15)泥炭及び/又は粘土カゝらなるマトリックスに、ァスコルビン酸及び鉄成分が含 有された粒状体からなることを特徴とするアルカリ土壌用植物用鉄供給剤。 (15) An iron supply agent for plants for alkaline soil, characterized by comprising a granular material containing ascorbic acid and an iron component in a matrix made of peat and / or clay.
(16)上記泥炭及び/又は粘土、上記ァスコルビン酸及び上記鉄成分として含有さ れた FeOの合計を 100質量0 /0とした場合に、該ァスコルビン酸は 1〜30質量0 /0であ り、該 FeOは 1〜30質量%である上記(15)に記載のアルカリ土壌用植物用鉄供給 剤。 (16) The peat and / or clay, the sum of the FeO which is contained as the Asukorubin acid and the iron component is 100 mass 0/0, the Asukorubin acid Ri 1-30 mass 0/0 der The Fe iron for alkaline soil plants according to (15) above, wherein the FeO is 1 to 30% by mass.
(17)ァスコルビン酸粉末と、鉄成分粉末と、水と、を含有する混合物を加熱して、 該ァスコルビン酸粉末及び該鉄成分粉末が溶解されて得られた水溶液を得る溶解 工程を備えることを特徴とするアルカリ土壌用植物用鉄供給剤の製造方法。 (17) A heating step comprising heating a mixture containing ascorbic acid powder, iron component powder, and water to provide an aqueous solution obtained by dissolving the ascorbic acid powder and the iron component powder. A method for producing a plant iron supply agent for alkaline soil.
(18)上記鉄成分粉末が鉄粉及び Z又は FeO粉末である上記(17)に記載のアル カリ土壌用植物用鉄供給剤の製造方法。 (18) The above-mentioned (17), wherein the iron component powder is iron powder and Z or FeO powder. The manufacturing method of the iron supply agent for plants for potash soil.
(19)上記鉄成分粉末が FeO粉末である上記(18)に記載のアルカリ土壌用植物 用鉄供給剤の製造方法。 (19) The method for producing an iron supply agent for a plant for alkaline soil according to (18), wherein the iron component powder is FeO powder.
(20)上記水溶液力 水を除去する乾燥工程を備える上記(17)に記載のアルカリ 土壌用植物用鉄供給剤の製造方法。 (20) The method for producing an iron supply agent for an alkaline soil plant according to the above (17), further comprising a drying step for removing water.
(21)上記 FeO粉末は、鉄分を含有するダストを造粒してなる造粒品、及び Z又は 鉄分を含有するダストと還元剤とを造粒してなる造粒品、を真空加熱したのち真空急 冷して得られた FeO粉末である上記(19)に記載のアルカリ土壌用植物用鉄供給剤 の製造方法。 (21) The above FeO powder is prepared by vacuum heating a granulated product obtained by granulating iron-containing dust and a granulated product obtained by granulating Z or iron-containing dust and a reducing agent. The method for producing an iron supply agent for a plant for alkaline soil according to the above (19), which is FeO powder obtained by vacuum quenching.
(22)上記(15)に記載のアルカリ土壌用植物用鉄供給剤の製造方法であって、 上記泥炭及び/又は粘土と、ァスコルビン酸粉末と、鉄成分粉末とを混合し、その後 (22) The method for producing an iron fertilizer for plants according to (15) above, wherein the peat and / or clay, ascorbic acid powder, and iron component powder are mixed,
、造粒することを特徴とするアルカリ土壌用植物用鉄供給剤の製造方法。 A method for producing an iron supply agent for a plant for alkaline soil, characterized by granulating.
(23)上記鉄成分粉末が鉄粉及び Z又は FeO粉末である上記(22)に記載のアル カリ土壌用植物用鉄供給剤の製造方法。 (23) The method for producing an iron supply agent for a plant for alkaline soil according to (22), wherein the iron component powder is iron powder and Z or FeO powder.
(24)上記鉄成分粉末が FeO粉末である上記(23)に記載のアルカリ土壌用植物 用鉄供給剤の製造方法。 (24) The method for producing an iron supply agent for an alkaline soil plant according to the above (23), wherein the iron component powder is FeO powder.
(25)上記泥炭及び/又は粘土、上記ァスコルビン酸粉末及び上記 FeO粉末の合 計を 100質量%とした場合に、該ァスコルビン酸粉末は 1〜30質量%であり、該 FeO 粉末は 1〜30質量%である上記(24)に記載のアルカリ土壌用植物用鉄供給剤の製 造方法。 (25) When the total of the peat and / or clay, the ascorbic acid powder and the FeO powder is 100% by mass, the ascorbic acid powder is 1 to 30% by mass, and the FeO powder is 1 to 30%. The manufacturing method of the iron supply agent for plants for alkaline soil as described in said (24) which is the mass%.
(26)上記 FeO粉末は、鉄分を含有するダストを造粒してなる造粒品、及び Z又は 鉄分を含有するダストと還元剤とを造粒してなる造粒品、を真空加熱したのち真空急 冷して得られた FeO粉末である上記(24)に記載のアルカリ土壌用植物用鉄供給剤 の製造方法。 (26) The above FeO powder is prepared by vacuum heating a granulated product obtained by granulating iron-containing dust and a granulated product obtained by granulating Z or iron-containing dust and a reducing agent. The method for producing an iron supply agent for a plant for alkaline soil according to the above (24), which is FeO powder obtained by vacuum quenching.
発明の効果 The invention's effect
ァスコルビン酸と鉄成分とが溶解されて得られた水溶液カゝらなる本発明のアルカリ 土壌用植物用鉄供給剤、及びァスコルビン酸と、鉄成分と、が溶解されて得られた水 溶液力も水を除去してなる他の本発明のアルカリ土壌用植物用鉄供給剤によれば、 特に鉄成分が FeOであるとき、高い Fe2+イオン濃度が得られる。即ち、例えば、土壌 中で水溶された場合にも高 、Fe2+イオン濃度を得ることができ、高 、確率で鉄分の 供給ができる。また、得られる Fe2+イオンは効果的に酸ィ匕が抑制されるため、高い確 率で鉄分の供給ができる。更に、ァスコルビン酸を使用しているために、環境負荷が なぐ使用上安全である。 An aqueous solution obtained by dissolving ascorbic acid and an iron component, and an aqueous solution obtained by dissolving ascorbic acid and an iron component. According to another iron supply agent for alkaline soil plants of the present invention obtained by removing Particularly when the iron component is FeO, obtained higher Fe 2+ ion concentration. That is, for example, even when water is dissolved in soil, a high Fe 2+ ion concentration can be obtained, and iron can be supplied with high probability. Further, the resulting Fe 2+ ions for effectively Sani spoon is suppressed, it is the supply of iron at a high probability. In addition, because it uses ascorbic acid, it is safe to use with no environmental impact.
また、鉄成分が FeOであり、所定の Fe2+イオン割合である場合は、特に高い確率 で鉄分の供給ができる。 In addition, when the iron component is FeO and has a predetermined Fe 2+ ion ratio, iron can be supplied with a particularly high probability.
更に、鉄成分が FeOであり、 pHが 7. 0以上の領域で測定し、その後、所定時間静 置後の Fe2+イオン濃度が測定開始直後の 80%以上である場合は、特に高 、抗酸 化性を有し、長期的に安定して Fe2+イオンを供給できる。 Furthermore, when the iron component is FeO and the pH is measured in the region of 7.0 or more, and then the Fe 2+ ion concentration after standing for a predetermined time is 80% or more immediately after the start of measurement, it is particularly high. It has antioxidant properties and can supply Fe 2+ ions stably over the long term.
また、生分解性バインダを含有する場合は、 Fe2+を長期間に亘つて安定して徐々 に供給する徐放性を有する植物用鉄供給剤とすることができる。 Moreover, when a biodegradable binder is contained, it can be set as the iron supply agent for plants which has the sustained release property which supplies Fe <2+ > stably and gradually over a long period of time.
更に、生分解性増量剤を含有する場合は、 Fe2+供給量を適当な範囲に簡便に保 つことができ、汎用性に優れる。 Furthermore, when a biodegradable extender is contained, the Fe 2+ supply amount can be easily kept within an appropriate range, and the versatility is excellent.
[0008] 泥炭及び/又は粘土カゝらなるマトリックスに、ァスコルビン酸及び鉄成分が含有され た粒状体からなる更に他の本発明のアルカリ土壌用植物用鉄供給剤によれば、特に 鉄成分が FeOであるとき、 Fe2+の酸化がより確実に抑制され、 Fe2+を特に安定して 徐々に供給する徐放性を有する植物用鉄供給剤とすることができる。 [0008] According to still another plant iron supplier for alkaline soil according to the present invention, the iron component for alkaline soil according to the present invention comprises a granular material in which ascorbic acid and an iron component are contained in a matrix made of peat and / or clay. When it is FeO, the oxidation of Fe 2+ is more reliably suppressed, and a plant iron supply agent having a sustained release property that supplies Fe 2+ particularly stably and gradually can be obtained.
更に、泥炭及び/又は粘土、ァスコルビン酸及び鉄成分として含有された FeOの合 計を 100質量%とした場合に、ァスコルビン酸が 1〜30質量%であり、 FeOが 1〜30 質量%である場合は、より確実に徐放性を有する植物用鉄供給剤とすることができる Furthermore, when the total amount of peat and / or clay, ascorbic acid and FeO contained as an iron component is 100% by mass, ascorbic acid is 1 to 30% by mass and FeO is 1 to 30% by mass. In this case, it is possible to obtain an iron supply agent for plants having more reliable sustained release.
[0009] 溶解工程を備える本発明の製造方法によれば、ァスコルビン酸と鉄成分とが溶解さ れて得られた水溶液カゝらなる前記本発明のアルカリ土壌用植物用鉄供給剤を安定し て、確実に得ることができる。 [0009] According to the production method of the present invention including the dissolution step, the plant iron supply agent for alkaline soil according to the present invention comprising the aqueous solution obtained by dissolving ascorbic acid and the iron component is stabilized. Can be obtained reliably.
また、水溶液力も水を除去する乾燥工程を備える場合は、ァスコルビン酸と鉄成分 とが溶解されて得られた水溶液力ゝら水を除去してなる前記他の本発明のアルカリ土 壌用植物用鉄供給剤を安定して、確実に得ることができる。 造粒工程を備える更に他の本発明の製造方法によれば、泥炭及び/又は粘土をマ トリックスとする徐放性を有するアルカリ土壌用植物用鉄供給剤を安定して、確実に 得ることができる。 In addition, when the aqueous solution is equipped with a drying process for removing water, the aqueous solution obtained by dissolving ascorbic acid and the iron component is used to remove water from the aqueous solution for alkaline soil plants of the present invention. An iron supply agent can be obtained stably and reliably. According to still another production method of the present invention including a granulation step, it is possible to stably and reliably obtain an iron supply agent for alkaline soil plants having a sustained release property using peat and / or clay as a matrix. it can.
また、泥炭及び/又は粘土、ァスコルビン酸粉末及び鉄成分粉末として配合された Also blended as peat and / or clay, ascorbic acid powder and iron component powder
FeO粉末の合計を 100質量%とした場合に、ァスコルビン酸粉末が 1〜30質量%で あり、 FeO粉末力^〜 30質量%である場合は、より確実に徐放性を有する植物用鉄 供給剤とすることができる。 When the total amount of FeO powder is 100% by mass, the ascorbic acid powder is 1-30% by mass, and the FeO powder power is 30% by mass. It can be used as an agent.
更に、本発明の製造方法、他の本発明の製造方法及び更に他の本発明の製造方 法において、鉄成分粉末が FeO粉末であり、この FeO粉末が造粒品を真空加熱した のち真空急冷して得られた FeO粉末である場合は、特に抗酸ィ匕性の高 、FeOを含 有する植物用鉄供給剤を確実に安定して得ることができる。 Further, in the production method of the present invention, another production method of the present invention, and still another production method of the present invention, the iron component powder is FeO powder, and this FeO powder is vacuum-quenched after the granulated product is heated in vacuum. In the case of the FeO powder obtained in this way, it is possible to reliably and stably obtain a plant iron supply agent that has particularly high acidity and contains FeO.
図面の簡単な説明 Brief Description of Drawings
圆 1]生分解性増量剤をマトリックスとする本他の植物用鉄供給剤を用いた実験例 7 のイネの生育状況を、肥料のみを用いたときの生育状況とともに示す説明図である。 圆 2]生分解性増量剤をマトリックスとする本他の植物用鉄供給剤を用いた実験例 9 〜16のイネの地上部の生育状況を、肥料のみを用いた実験例 8の生育状況とともに 示す説明図である。 圆 1] It is explanatory drawing which shows the growth condition of the rice of Experimental example 7 using the other iron supply agent for plants which uses a biodegradable extender as a matrix with the growth condition when using only a fertilizer.圆 2] Experiments using other plant iron suppliers with biodegradable extender as matrix The growth of the above-ground part of rice in 9 to 16 together with the growth of Experiment 8 using only fertilizer It is explanatory drawing shown.
[図 3]肥料のみを用いた実験例 8の地上部の生育状況と、実験例 9、 10のイネの地上 部の生育状況とを比較して示す説明図である。 FIG. 3 is an explanatory diagram showing a comparison of the growth situation of the above-ground part of Experimental Example 8 using only fertilizer and the growth situation of the above-ground part of rice of Experimental Examples 9 and 10.
[図 4]肥料のみを用いた実験例 8の地上部の生育状況と、実験例 11、 12のイネの地 上部の生育状況とを比較して示す説明図である。 FIG. 4 is an explanatory diagram showing a comparison of the growth situation of the above-ground part of Experimental Example 8 using only fertilizer and the growth situation of the upper part of the rice of Experimental Examples 11 and 12.
[図 5]肥料のみを用いた実験例 8の地上部の生育状況と、実験例 13、 14のイネの地 上部の生育状況とを比較して示す説明図である。 FIG. 5 is an explanatory view showing a comparison of the growth situation of the above-ground part of Experimental Example 8 using only fertilizer and the growth situation of the upper part of the rice of Experimental Examples 13 and 14.
[図 6]肥料のみを用いた実験例 8の地上部の生育状況と、実験例 15、 16のイネの地 上部の生育状況とを比較して示す説明図である。 FIG. 6 is an explanatory diagram showing a comparison of the growth situation of the above-ground part of Experimental Example 8 using only fertilizer and the growth situation of the upper part of the rice of Experimental Examples 15 and 16.
圆 7]生分解性増量剤をマトリックスとする本他の植物用鉄供給剤を用いた実験例 9 〜16のイネの根部の生育状況を、肥料のみを用いた実験例 8の生育状況とともに示 す説明図である。 [図 8]肥料のみを用いた実験例 8の地上部の生育状況と、実験例 9、 10のイネの根部 の生育状況とを比較して示す説明図である。 圆 7] Experiments using other plant iron suppliers with biodegradable extenders as matrixes Show the growth of rice roots in Examples 9 to 16 together with the growth of Experiment 8 using only fertilizer FIG. FIG. 8 is an explanatory diagram showing a comparison of the growth situation of the above-ground part in Experimental Example 8 using only fertilizer and the growth situation of the root part of rice in Experimental Examples 9 and 10.
[図 9]肥料のみを用いた実験例 8の地上部の生育状況と、実験例 11、 12のイネの根 部の生育状況とを比較して示す説明図である。 FIG. 9 is an explanatory diagram showing a comparison of the growth situation of the above-ground part in Experimental Example 8 using only fertilizer and the growth situation of the root part of rice in Experimental Examples 11 and 12.
[図 10]肥料のみを用いた実験例 8の地上部の生育状況と、実験例 13、 14のイネの根 部の生育状況とを比較して示す説明図である。 FIG. 10 is an explanatory diagram showing a comparison of the growth situation of the above-ground part in Experimental Example 8 using only fertilizer and the growth situation of the root part of rice in Experimental Examples 13 and 14.
[図 11]肥料のみを用いた実験例 8の地上部の生育状況と、実験例 15、 16のイネの根 部の生育状況とを比較して示す説明図である。 FIG. 11 is an explanatory diagram showing a comparison of the growth situation of the above-ground part in Experimental Example 8 using only fertilizer and the growth situation of the root part of rice in Experimental Examples 15 and 16.
発明を実施するための最良の形態 BEST MODE FOR CARRYING OUT THE INVENTION
[0011] 以下、本発明を詳細に説明する。 Hereinafter, the present invention will be described in detail.
[1]アルカリ土壌用植物用鉄供給剤 [1] Plant iron supply for alkaline soil
本発明のアルカリ土壌用植物用鉄供給剤 (以下、単に「本植物用鉄供給剤」 t ヽぅ 。)は、ァスコルビン酸と、鉄成分と、が溶解されて得られた水溶液からなることを特徴 とする。 The plant iron supply agent for alkaline soil according to the present invention (hereinafter simply “the iron supply agent for plants” t t) is composed of an aqueous solution obtained by dissolving ascorbic acid and an iron component. Features.
他の本発明のアルカリ土壌用植物用鉄供給剤 (以下、単に「本他の植物用鉄供給 剤」という。)は、ァスコルビン酸と、鉄成分と、が溶解されて得られた水溶液力も水を 除去してなることを特徴とする。即ち、本他の植物用鉄供給剤は、上記本植物用鉄 供給剤から水を除去して得られる。 Another plant iron supplier for alkaline soil of the present invention (hereinafter simply referred to as “the other plant iron supplier”) has an aqueous solution obtained by dissolving ascorbic acid and an iron component. It is characterized by removing. That is, the other iron supply agent for plants can be obtained by removing water from the iron supply agent for plants.
更に他の本発明のアルカリ土壌用植物用鉄供給剤(以下、単に「本更に他の植物 用鉄供給剤」という。)は、泥炭及び/又は粘土力もなるマトリックスに、ァスコルビン酸 及び鉄成分が含有された粒状体からなることを特徴とする。 Still another plant iron supply agent for alkaline soil according to the present invention (hereinafter simply referred to as “this further iron supply agent for plants”) contains peat and / or a matrix that also has clay power, ascorbic acid and an iron component. It consists of the contained granular material, It is characterized by the above-mentioned.
[0012] 上記の各発明におけるアルカリ土壌とは、風燥した土壌 10gに蒸留水 25ミリリットル をカロえて 1時間振とうし、得られた懸濁液の pHを測定した場合に、その pHが 7を越え る土壌のことをいう。従って、このアルカリ土壌には、本来的なアルカリ土壌及び非ァ ルカリ土壌が後天的に、例えば、施肥、砂漠ィ匕等によりアルカリィ匕してなるアルカリ土 壌が含まれる。上記の本来的なアルカリ土壌としては、貝化石土壌、石灰質土壌、珊 瑚質土壌等の各種石灰質成分が含まれる土壌が挙げられる。これらは 1種のみ用い てもよく、 2種以上を併用してもよい。更に、これらの各種石灰質成分が含まれるアル カリ土壌と、非アルカリ土壌との混合土壌であって、全体としてアルカリ土壌であるも のち含まれる。 [0012] Alkaline soil in each of the above inventions means that when 10g of air-dried soil is charged with 25ml of distilled water and shaken for 1 hour and the pH of the resulting suspension is measured, the pH is 7 This refers to soil that exceeds the threshold. Accordingly, the alkaline soil includes alkaline soil obtained by alkaline conversion of the original alkaline soil and non-alkali soil, for example, by fertilization, desert rehabilitation, or the like. Examples of the above basic alkaline soil include soils containing various calcareous components such as shell fossil soil, calcareous soil, and clay soil. These may be used alone or in combination of two or more. In addition, these various calcareous components It is a mixed soil of potash soil and non-alkaline soil, and it is included after being alkaline soil as a whole.
[0013] また、上記の各発明における「鉄成分」は特に限定されず、鉄化合物でもよぐ鉄粉 等の金属鉄でもよい。鉄化合物は特に限定されないが、分子内に 2価鉄を有する化 合物がより好ましい。この鉄化合物としては、例えば、 FeO等の酸化物、 FeSO、 Fe In addition, the “iron component” in each of the above inventions is not particularly limited, and may be metallic iron such as iron powder, which may be an iron compound. The iron compound is not particularly limited, but a compound having divalent iron in the molecule is more preferable. Examples of the iron compound include oxides such as FeO, FeSO, Fe
4 Four
(NO ) 、 FeCl等の無機塩、トリメトキシ鉄等の有機塩及び Fe— EDTA、 Fe— ED(NO), inorganic salts such as FeCl, organic salts such as trimethoxy iron and Fe-EDTA, Fe-ED
3 2 2 3 2 2
DHA等のキレートイ匕合物などが挙げられる。この鉄化合物としては FeOが特に好ま しい。鉄化合物は 1種のみ用いてもよぐ 2種以上を併用してもよい。更に、金属鉄と 1 種以上の鉄化合物とを併用してもよい。鉄成分は、金属鉄及び Z又は FeOであるこ と力 S好ましく、 FeOであることがより好ましい。 Examples include chelate compounds such as DHA. As this iron compound, FeO is particularly preferred. Only one type of iron compound may be used, or two or more types may be used in combination. Further, metallic iron and one or more iron compounds may be used in combination. The iron component is metallic iron and Z or FeO, preferably S, more preferably FeO.
[0014] (1)本植物用鉄供給剤 [0014] (1) Iron supply agent for this plant
上記「ァスコルビン酸」は、ヒドロキシル基を有する有機酸である。このァスコルビン 酸は刺激臭がなぐまた、ァスコルビン酸と鉄成分とを含有する水溶液を調製した場 合に、ァスコルビン酸濃度に対する Fe2+イオン濃度を高くすることができる。 The “ascorbic acid” is an organic acid having a hydroxyl group. This ascorbic acid has no irritating odor. When an aqueous solution containing ascorbic acid and an iron component is prepared, the Fe 2+ ion concentration relative to the ascorbic acid concentration can be increased.
[0015] 上記「水溶液」は、ァスコルビン酸と鉄成分とが溶解されて得られた水溶液である。 [0015] The "aqueous solution" is an aqueous solution obtained by dissolving ascorbic acid and an iron component.
即ち、溶解しきらな ヽァスコルビン酸及び溶解しきらな ヽ鉄成分が含有されな 、水溶 液である。但し、この水溶液は、溶解しきらないァスコルビン酸及び/又は溶解しきら な 、鉄成分が含有される固液共存物中における上澄み液であってもよ 、。 That is, it is an aqueous solution that does not contain easily dissolved ascorbic acid and not easily dissolved pig iron component. However, this aqueous solution may be a supernatant in a solid-liquid coexisting material containing ascorbic acid and / or an iron component that cannot be dissolved.
また、ァスコルビン酸及び鉄成分の水溶液中における溶解状態は特に限定されな い。即ち、例えば、この水溶液にはァスコルビン酸鉄錯体及びァスコルビン酸イオン 等を含有できる。これらのなかでも特にァスコルビン酸鉄錯体が含有されることが好ま しい。 Further, the dissolved state of ascorbic acid and the iron component in the aqueous solution is not particularly limited. That is, for example, the aqueous solution of ascorbate and ascorbate ions can be contained in this aqueous solution. Among these, it is particularly preferred that an iron ascorbate complex is contained.
[0016] この水溶液に溶解されたァスコルビン酸の量は特に限定されないが、通常、水 100 mlあたりのァスコルビン酸は 0. 05g以上(好ましくは 0. 5g〜水溶液の温度における ァスコルビン酸の溶解度)である。一方、鉄成分は、ァスコルビン酸を 100質量部とし た場合に、 10〜25質量部、特に 20〜25質量部配合することができる。 [0016] The amount of ascorbic acid dissolved in this aqueous solution is not particularly limited. Usually, the amount of ascorbic acid per 100 ml of water is 0.05 g or more (preferably 0.5 g to the solubility of ascorbic acid at the temperature of the aqueous solution). is there. On the other hand, the iron component can be added in an amount of 10 to 25 parts by mass, particularly 20 to 25 parts by mass, with ascorbic acid being 100 parts by mass.
[0017] また、この水溶液を構成する水は、特に限定されず、種々の水を用いることができる 。純水及びイオン交換水等の高度に精製された水であってもよぐ水道水、工業用水 、農業用水及び地下水等の通常使用される水であってもよい。 [0017] The water constituting the aqueous solution is not particularly limited, and various types of water can be used. Tap water and industrial water that can be highly purified water such as pure water and ion exchange water Ordinarily used water such as agricultural water and groundwater may be used.
[0018] この水溶液を得る方法は特に限定されないが、後述する製造方法により得ることが できる。即ち、(1)ァスコルビン酸粉末と、鉄成分粉末と、水と、を含有する混合物を 加熱して得ることができる。その他、(2)予め全量を溶解させたァスコルビン酸水溶液 に、鉄成分粉末を添加し、加熱して得ることもできる。また、(3)予め所定量を溶解さ せたァスコルビン酸水溶液に、更にァスコルビン酸粉末と鉄成分粉末とを添加し、加 熱して得ることもできる。更に、(4)加熱せずァスコルビン酸粉末と鉄成分粉末と水と を混合して得ることもできる。また、(5)上記(1)〜 (4)に加えて溶解して ヽな ヽァスコ ルビン酸及び溶解して 、な 、FeOが含有される場合は、これらを濾過等の方法で分 離する工程を備える製造方法とすることができる。 [0018] The method for obtaining this aqueous solution is not particularly limited, but can be obtained by a production method described later. That is, it can be obtained by heating a mixture containing (1) ascorbic acid powder, iron component powder, and water. In addition, (2) it can also be obtained by adding an iron component powder to an ascorbic acid aqueous solution in which the entire amount is dissolved in advance and heating. Alternatively, (3) an ascorbic acid powder and an iron component powder may be further added to an ascorbic acid aqueous solution in which a predetermined amount is dissolved in advance and heated. Furthermore, (4) it can be obtained by mixing ascorbic acid powder, iron component powder and water without heating. Further, (5) in addition to the above (1) to (4), when dissolved, lascosulvic acid and dissolved, and when FeO is contained, these are separated by a method such as filtration. It can be set as the manufacturing method provided with a process.
[0019] 本植物用鉄供給剤は、防黴のために木酢液を含有させることができる。木酢液を含 有させる場合、木酢液の含有量は本植物用鉄供給剤全体の 10質量%以下 (通常、 5質量%以上)が好ましい。更に、同様な目的で予め紫外線照射を行うことができる。 紫外線照射条件等は特に限定されないが、波長 200〜380nmの紫外線を用いるこ とが好ましい。また、照射を行う場合には 72 X 10 w' s/cm2以上を照射すること が好ましい。更に、保存の際には低温で保存することが好ましい。その温度は特に限 定されな!/ヽが 15°C以下が好ま ヽ。 [0019] The plant iron supply agent may contain a pyroligneous acid solution for fungicide. When the wood vinegar is included, the content of the wood vinegar is preferably 10% by mass or less (usually 5% by mass or more) of the whole iron supply agent for plants. Furthermore, ultraviolet irradiation can be performed in advance for the same purpose. Although the ultraviolet irradiation conditions are not particularly limited, it is preferable to use ultraviolet rays having a wavelength of 200 to 380 nm. When irradiation is performed, it is preferable to irradiate 72 × 10 w ′s / cm 2 or more. Furthermore, when storing, it is preferable to store at a low temperature. The temperature is not particularly limited! / ヽ is preferably 15 ° C or less.
本植物用鉄供給剤の性質につ!、ては後述する。 The nature of the iron supply agent for plants will be described later.
[0020] (2)本他の植物用鉄供給剤 [0020] (2) Other iron supply agents for plants
本他の植物用鉄供給剤は、上記水溶液力 水を除去して得られる。 This other iron supply agent for plants is obtained by removing the aqueous solution water.
上記「除去」は、水溶液から水の一部又は全部を除去する作業を意味するが、通常 、本他の植物用鉄供給剤全体に対する水分量は 90質量%以下である。特に固形物 では水分量は 10質量%以下 (好ましくは 5質量%以下)であり、ペースト状物では水 分量は 60〜90質量% (好ましくは 65〜85質量%)である。本他の植物用鉄供給剤 は、水溶液から実質的に全部の水が除去された固形物であってもよぐ水溶液から 一部の水が除去されたペースト状物であってもよいが、これらのうちでは固形物が好 ましい。 The above “removal” means an operation of removing a part or all of water from the aqueous solution, but usually the water content with respect to the whole other iron supply agent for plants is 90% by mass or less. In particular, the water content is 10% by mass or less (preferably 5% by mass or less) for solid materials, and the water content is 60 to 90% by mass (preferably 65 to 85% by mass) for pastes. The other iron supply agent for plants may be a solid material from which substantially all water has been removed from the aqueous solution, or may be a paste-like material from which some water has been removed from the aqueous solution. Of these, solids are preferred.
また、この水の除去方法は特に限定されず、減圧加熱乾燥、常圧加熱乾燥、非力口 熱減圧乾燥、及び凍結乾燥等の手段を用いることができる。これらのなかでは、減圧 加熱乾燥が好ま 、。この水を除去する過程で Fe2+が酸ィ匕されることを抑制できるか らである。また、減圧乾燥以外にも、低酸素分圧下における乾燥でもよい。 The method for removing the water is not particularly limited, and drying under reduced pressure, drying under normal pressure, Means such as thermal vacuum drying and freeze-drying can be used. Of these, vacuum drying is preferred. This is because it is possible to suppress the oxidation of Fe 2+ during the process of removing water. In addition to drying under reduced pressure, drying under a low oxygen partial pressure may be used.
[0021] 水を除去する際に加熱する場合、水溶液の温度は特に限定されないが、 120°C以 下に保持することが好ましい。 120°Cを超えると Fe3+イオン濃度が高くなる傾向にあ る力らである。この加熱による水溶液の温度は、 100°C以下がより好ましぐ 90°C以 下が更に好ましぐ 70°C以下が特に好ましい。一方、下限温度は特に限定されず、 水を除去する際の圧力下で水の蒸散を生じる温度であればよい。水溶液の温度は、 例えば、 45°C以上が好ましぐ 50°C以上がより好ましぐ 55°C以上が更に好ましぐ 6 0°C以上が特に好ましぐ 65°C以上がとりわけ好ましい。これらの加熱の際の上限温 度及び下限温度は各々組合せとすることができる。即ち、例えば、 45〜120°Cが好 ましぐ 50〜100°Cがより好ましぐ 60〜70°Cが更に好ましい。これら以外の組合せ であってもよい。 [0021] When heating at the time of removing water, the temperature of the aqueous solution is not particularly limited, but is preferably maintained at 120 ° C or lower. When the temperature exceeds 120 ° C, the Fe 3+ ion concentration tends to increase. The temperature of the aqueous solution by this heating is particularly preferably 100 ° C. or less, more preferably 90 ° C. or less, and further preferably 70 ° C. or less. On the other hand, the lower limit temperature is not particularly limited, and may be any temperature that causes transpiration of water under the pressure when removing water. The temperature of the aqueous solution is, for example, preferably 45 ° C or higher, more preferably 50 ° C or higher, more preferably 55 ° C or higher, particularly preferably 60 ° C or higher, and particularly preferably 65 ° C or higher. . These upper limit temperature and lower limit temperature in the heating can be combined. That is, for example, 45 to 120 ° C is preferable, 50 to 100 ° C is more preferable, and 60 to 70 ° C is more preferable. Combinations other than these may be used.
[0022] 更に、水を除去する際に減圧にする場合、その圧力は特に限定されないが、 0. 1 〜50kPa力 S好ましく、 0. l〜20kPa力 Sより好ましく、 3〜15kPa力更に好ましく、 4〜1 OkPaが特に好ましい。 [0022] Further, when reducing the pressure when removing water, the pressure is not particularly limited, but is preferably 0.1 to 50 kPa force S, more preferably 0.1 to 20 kPa force S, more preferably 3 to 15 kPa force, 4 to 1 OkPa is particularly preferred.
[0023] 本他の植物用鉄供給剤は、通常、 15°C以上の温度の水にほぼ全量を溶解させる ことができる。例えば、温度 25°Cの純水 100mlに対しては 0. lg以上(更には 0. 1〜 120g、特に 0. l〜50g、とりわけ 0. l〜15g)を溶解させること力できる。この本他の 植物用鉄供給剤を溶解させた水溶液の性質については後述する。 [0023] In general, the other iron supply agents for plants can be dissolved almost entirely in water having a temperature of 15 ° C or higher. For example, it is possible to dissolve 0.1 lg or more (further 0.1 to 120 g, particularly 0.1 to 50 g, especially 0.1 to 15 g) in 100 ml of pure water at a temperature of 25 ° C. The properties of the aqueous solution in which this other iron supply agent for plants is dissolved will be described later.
この本他の植物用鉄供給剤におけるァスコルビン酸、水溶液、水及び防黴のため の処理等については、前記本植物用鉄供給剤における各々の記載をそのまま適用 できる。 Regarding the treatment for ascorbic acid, aqueous solution, water, and fungicides in this other iron supply agent for plants, the descriptions in the iron supply agent for plants can be applied as they are.
[0024] 本他の植物用鉄供給剤の使用方法も特に限定されな!ヽ。例えば、土と混合 (粉体 状で、塊状で)する、土に散布 (粉体状で)する、土中に埋める (粉体状で、塊状で) 等の使用方法が挙げられる。 [0024] The method of using the other iron supply agent for plants is not particularly limited. For example, it can be mixed with soil (powdered or lump), sprayed on soil (powdered), or buried in soil (powdered or lump).
[0025] (3)本植物用鉄供給剤及び本他の植物用鉄供給剤に共通する事項 [0025] (3) Items common to the plant iron supply agent and other plant iron supply agents
本植物用鉄供給剤及び本他の植物用鉄供給剤を水溶させた水溶液には、それぞ れ Fe2+イオンと Fe3+イオンとが含有され、特に鉄成分が FeOである場合、 Fe +ィォ ンと Fe3+イオンとの合計を 100質量0 /0とした場合に、 Fe2+イオンが 50〜99質量0 /0 ( 更には 60〜90質量%、特に 70〜90質量%)含有される。即ち、 Fe3+イオンは 1〜5 0質量% (更には 10〜40質量%、特に 10〜30質量%)含有される。即ち、高濃度に Fe2+を含有する水溶液を得ることができる。但し、この Fe2+イオン濃度は、後述する 実施例の測定方法により測定された値である。また、 Fe3+イオン濃度は、鉄供給剤を 濃度 10gZリットル (約 1. 0質量%)となるように温度 20°Cのイオン交換水に撹拌混 合して溶解させ (およそ 5分間撹拌)、その後、メンブランフィルター(孔径 1 μ m)を用 いて濾過し、濾過後、直ちに紫外 ·可視光分光光度計 (株式会社島津製作所製、形 式「UV1240」)に水質測定パックを装着して、水溶液に含有される Fe2+イオン量及 び総 Feイオン量を測定し、この総 Feイオン量力も Fe2+イオン量を差し引 、て算出し た。 The aqueous solution in which the plant iron supply agent and other plant iron supply agents are dissolved in water, Re is a Fe 2+ ions and Fe 3+ ions are contained, especially if the iron component is FeO, when the total of the Fe + I O emissions and Fe 3+ ions is 100 mass 0/0, Fe 2 + ions 50 to 99 mass 0/0 (even 60-90% by weight, in particular 70 to 90 wt%) is contained. That, Fe 3+ ions 1-5 0% by weight (still more 10 to 40% by weight, in particular 10 to 30 wt%) is contained. That is, an aqueous solution containing Fe 2+ at a high concentration can be obtained. However, this Fe 2+ ion concentration is a value measured by the measurement method of the example described later. The Fe 3+ ion concentration is dissolved by stirring and mixing in ion-exchanged water at a temperature of 20 ° C so that the concentration of the iron supply agent is 10 gZ liter (about 1.0% by mass) (stir for about 5 minutes). Then, filter using a membrane filter (pore size 1 μm). Immediately after filtration, attach a water quality measurement pack to an ultraviolet / visible light spectrophotometer (Shimadzu Corporation, model “UV1240”). The amount of Fe 2+ ions and the total amount of Fe ions contained in the aqueous solution were measured, and the total amount of Fe ions was also calculated by subtracting the amount of Fe 2+ ions.
[0026] また、本植物用鉄供給剤及び本他の植物用鉄供給剤の各々を溶解させた水溶液 では、特に鉄成分力 SFeOである場合、それぞれ pHが 7. 0以上の領域で Fe2+イオン 濃度 (mgZリットル)を測定し、その後、 120時間静置し、再び測定した Fe2+イオン濃 度が、静置前の Fe2+イオン濃度の 80%以上である。即ち、長期間安定して Fe2+ィォ ンを保持することができ、 Fe3+へ酸化されることが抑制された抗酸ィ匕性に優れた鉄供 給剤である。但し、上記静置は実質的に紫外線があたらない温度 25°Cの暗所にお けるものとする。この Fe2+イオン含有量は、後述する実施例の測定方法により測定し た値である。 [0026] In addition, in the aqueous solution in which each of the plant iron supply agent and the other plant iron supply agents is dissolved, particularly in the case where the iron component strength is SFeO, Fe 2 in the region where the pH is 7.0 or more. + ions to determine the concentration (MGZ liters), then allowed to stand for 120 hours, the measured Fe 2+ ion concentration again, at least 80% of the Fe 2+ ion concentration of an置前. In other words, it is an iron supply agent that can stably hold Fe 2+ ions for a long period of time and is excellent in anti-oxidation properties that are suppressed from being oxidized to Fe 3+ . However, the above standing shall be in a dark place at a temperature of 25 ° C where it is not exposed to UV rays. This Fe 2+ ion content is a value measured by the measurement method of Examples described later.
[0027] また、本植物用鉄供給剤及び本他の植物用鉄供給剤は、生分解性バインダを含 有することができる。生分解性バインダを含有することにより、このバインダが分解さ れるに従って徐々に鉄供給剤が放出されて Fe2+を生じる。このため長期に亘つて安 定して Fe2+イオンを供給することができる。即ち、本植物用鉄供給剤及び本他の植 物用鉄供給剤に徐放性を付与できる。 [0027] Further, the plant iron supply agent and the other plant iron supply agents may contain a biodegradable binder. By containing a biodegradable binder, the iron supply is gradually released as the binder is decomposed to produce Fe 2+ . Therefore, it is possible to supply Fe 2+ ions stably over a long period of time. That is, sustained release can be imparted to the plant iron supply agent and the other plant iron supply agents.
この生分解性バインダとしては、生分解性プラスチックを用いることができる。生分 解性プラスチックとしてはポリブチレンサクシネート系榭脂、ポリ乳酸系榭脂、尿素榭 脂、ポリ力プロラタトン系榭脂、セルロース系榭脂、澱粉系榭脂、ポリビュルアルコー ル系榭脂等が挙げられる。これらは 1種のみを用いてもよぐ 2種以上を併用してもよ い。 As the biodegradable binder, a biodegradable plastic can be used. Biodegradable plastics include polybutylene succinate-based resin, polylactic acid-based resin, urea resin, poly-strength prolatatone-based resin, cellulose-based resin, starch-based resin, and polybut alcohol. And the like. These may be used alone or in combination of two or more.
この生分解性バインダの含有量は特に限定されな 、が、本植物用鉄供給剤及び 本他の植物用鉄供給剤全体を 100質量%とした場合に 10質量%以下 (より好ましく は 2〜7質量%、通常 1質量%以上)とすることが好ましい。 The content of the biodegradable binder is not particularly limited. However, when the total amount of the iron supply agent for plants and the other iron supply agent for plants is 100% by mass, 10% by mass or less (more preferably 2 to 7% by mass, usually 1% by mass or more).
[0028] また、本植物用鉄供給剤及び本他の植物用鉄供給剤は、生分解性増量剤を含有 することができる。生分解性増量剤は、生分解性を有する上記バインダ以外の成分 である。この生分解性増量剤としては、籾殻、雪花菜、糠、焼酎粕、酒粕、タエン酸粕 、葦、泥炭、腐葉土、鶏糞、堆肥、牛糞及び骨粉等が挙げられる。これらは 1種のみ を用いてもよぐ 2種以上を併用してもよい。尚、生分解性増量剤は、植物に対する所 定の機能を有していてもよぐ有していなくてもよい。所定の機能を有する成分とは、 例えば、植物に対して栄養分となる成分が挙げられる。 [0028] Further, the plant iron supply agent and the other plant iron supply agents may contain a biodegradable extender. The biodegradable extender is a component other than the above binder having biodegradability. Examples of this biodegradable bulking agent include rice husk, snow flora, rice bran, shochu, sake lees, taenic acid lees, straw, peat, humus, chicken manure, compost, cow manure and bone meal. These may be used alone or in combination of two or more. The biodegradable extender may or may not have a predetermined function for plants. Examples of the component having a predetermined function include components that serve as nutrients for plants.
この生分解性増量剤の含有量は特に限定されな ヽが、本植物用鉄供給剤及び本 他の植物用鉄供給剤全体を 100質量%とした場合に 50〜94質量% (好ましくは 70 〜94質量%)とすることができる。この範囲であれば、多量の土に対して微量の植物 用鉄供給剤を混合した場合にも、適切な量を混合することができる。 The content of the biodegradable extender is not particularly limited, but it is 50 to 94% by weight (preferably 70% when the total amount of the iron supply agent for plants and other iron supply agents for plants is 100% by weight). ~ 94 mass%). Within this range, an appropriate amount can be mixed even when a small amount of plant iron supplier is mixed with a large amount of soil.
[0029] 本植物用鉄供給剤及び本他の植物用鉄供給剤は、生分解性バインダ及び生分解 性増量剤以外にも他の成分を含有することができる。他の成分としては、リポ酸、オリ ザ油、各種ビタミン類、 Mn、 Zn、 Cu、 Cr、 Si、 Mg、 Ca、 Co、 Mo、 Ni、 B等の各成 分 (例えば、金属状態、金属酸ィ匕物等)、 S及び C1等の化合物等が挙げられる。これ らは 1種のみを用いてもよぐ 2種以上を併用してもよい。その他の成分は、本植物用 鉄供給剤及び本他の植物用鉄供給剤に含有される生分解性バインダと生分解性増 量剤との合計を 100質量部とした場合に 10質量部以下とすることが好ましい。 [0029] The plant iron supply agent and the other plant iron supply agents may contain other components in addition to the biodegradable binder and the biodegradable extender. Other components include lipoic acid, oryza oil, various vitamins, Mn, Zn, Cu, Cr, Si, Mg, Ca, Co, Mo, Ni, B, etc. (for example, metallic state, metallic Acid compounds), and compounds such as S and C1. These may be used alone or in combination of two or more. The other ingredients are 10 parts by mass or less when the total of the biodegradable binder and biodegradable extender contained in the plant iron supplier and other plant iron supplier is 100 parts by mass. It is preferable that
[0030] 本植物用鉄供給剤及び本他の植物用鉄供給剤の使用方法は特に限定されない。 [0030] The method for using the plant iron supply agent and the other plant iron supply agents is not particularly limited.
例えば、液状である場合は、散布する(土、対象植物の根元等へ灌水、葉面散布等) 、浸漬する (水耕栽培用の培養液等として使用、対象植物の根を浸漬する等)、土に 混合する等の使用方法が挙げられる。また、固形状である場合は、土と混合 (粉体状 で、塊状で)する、土に散布 (粉体状で)する、土中に埋める (粉体状で、塊状で)等 の使用方法が挙げられる。 For example, if it is in liquid form, spray it (irrigate the soil, the root of the target plant, foliar spray, etc.) or immerse it (use it as a culture solution for hydroponics, soak the root of the target plant, etc.) , And use method such as mixing with soil. If solid, mix with soil (powder, lump), spread on soil (powder), fill in soil (powder, lump), etc. The usage method is mentioned.
[0031] (4)生分解性増量剤をマトリックスとする本更に他の植物用鉄供給剤 [0031] (4) Still another iron supply agent for plants using a biodegradable extender as a matrix
生分解性増量剤をマトリックスとする更に本他の植物用鉄供給剤には、生分解性増 量剤のうちでも特に泥炭及び Z又は粘土が含有される。これらの生分解性増量剤は 撥水性であり、本更に他の植物用鉄供給剤をアルカリ土壌において用いたときに、 周囲からの pHの高い水溶液等の本更に他の植物用鉄供給剤への侵入が抑制され 、 pHが低く保たれるため、 FeOの溶解性の低下が抑えられ、且つ Fe2+イオンの酸ィ匕 もより抑制される。そのため、長期に亘つて安定して Fe2+イオンを供給することができ る。即ち、本更に他の植物用鉄供給剤により優れた徐放性を付与できる。 In addition to other biodegradable extenders, peat and Z or clay are contained in the other iron supply agents for plants using a biodegradable extender as a matrix. These biodegradable extenders are water-repellent, and when this other plant iron supply is used in alkaline soil, it can be used as an aqueous solution with a high pH from the surroundings. As the pH is kept low, the decrease in solubility of FeO is suppressed, and the acidity of Fe 2+ ions is further suppressed. Therefore, Ru can be supplied to prolonged connexion stable Fe 2+ ions. That is, excellent sustained release properties can be imparted by the present other iron supply agent for plants.
[0032] また、この本更に他の植物用鉄供給剤は、撥水性を有する生分解性増量剤である 泥炭及び Z又は粘土力もなるマトリックスに、ァスコルビン酸及び鉄成分が含有され た粒状体からなる。この粒状体を構成する粒子の形状は特に限定されず、球体、楕 円体、半球体、立方体、直方体、円柱体及びプリケット等のいずれでもよい。更に、 粒状体は緻密体でもよぐ多孔質体であってもよい。また、その粒径 (球体であるとき は直径、その他の形状であるときは最大差し渡し寸法)は 50mm以下 (より好ましくは 10mm以下、更に好ましくは 6mm以下、通常 0. 5mm以上)が好ましい。 [0032] Further, this other iron supply agent for plants includes a biodegradable extender having water repellency, peat and Z, or a granule containing ascorbic acid and an iron component in a matrix having clay power. Become. The shape of the particles constituting the granular body is not particularly limited, and may be any of a sphere, an ellipsoid, a hemisphere, a cube, a cuboid, a cylinder, a plecket, and the like. Further, the granular body may be a dense body or a porous body. In addition, the particle size (diameter in the case of a sphere, maximum interstitial dimension in the case of other shapes) is preferably 50 mm or less (more preferably 10 mm or less, further preferably 6 mm or less, usually 0.5 mm or more).
[0033] 更に、生分解性増量剤をマトリックスとする本更に他の植物用鉄供給剤では、ァス コルビン酸、鉄成分として含有された FeO並びに生分解性増量剤である泥炭及び/ 又は粘土の合計を 100質量%とした場合に、ァスコルビン酸は 1〜30質量%含有さ れ、 FeOは 1〜30質量0 /0含有されていることが好ましい。このァスコルビン酸の含有 量は 3〜20質量%、特に 7〜13質量%であることがより好ましぐ FeOの含有量は 3 〜20質量%、特に 7〜8質量%であることがより好ましい。これにより、 FeOの溶解性 の低下が十分に抑えられ、且つ Fe2+イオンの酸化もより十分に抑制され、長期に亘 つて安定して Fe2+イオンを供給することができる。 [0033] Furthermore, in this other iron supply agent for plants using a biodegradable extender as a matrix, ascorbic acid, FeO contained as an iron component, and peat and / or clay as biodegradable extenders. total is 100% by weight, Asukorubin acid is contained 1 to 30 wt%, FeO is preferably are contained 1-30 wt 0/0. The content of this ascorbic acid is more preferably 3 to 20% by mass, particularly preferably 7 to 13% by mass. The content of FeO is more preferably 3 to 20% by mass, particularly preferably 7 to 8% by mass. . Thus, reduction in the solubility of FeO is sufficiently suppressed, and the oxidation of Fe 2+ ions is more sufficiently suppressed, prolonged connexion can be stably supplied to Fe 2+ ions.
[0034] 上記のように、撥水性の生分解性増量剤により、ァスコルビン酸及び FeO等の鉄成 分と、外部環境との接触を抑制することにより、本更に他の植物用鉄供給剤をアル力 リ土壌において用いたときに、粒状体の内部の pHの上昇が抑えられる。これにより F eOの溶解性の低下が抑えられる。更に、空気中の酸素等によるァスコルビン酸の酸 ィ匕も抑制されるため、このァスコルビン酸による FeO等の鉄成分の酸ィ匕抑制の効果も 併せて得られ、長期に亘つてより安定して Fe2+イオンを供給することができる。 [0034] As described above, the water-repellent biodegradable extender suppresses the contact of iron components such as ascorbic acid and FeO with the external environment, thereby further reducing other plant iron supply agents. When used in Al soil, the increase in pH inside the granular material is suppressed. This suppresses the decrease in the solubility of FeO. Furthermore, the acid of ascorbic acid due to oxygen in the air As a result, the effect of ascorbic acid on the suppression of the acid content of iron components such as FeO can be obtained, and Fe 2+ ions can be supplied more stably over a long period of time.
[0035] 生分解性増量剤をマトリックスとした本更に他の植物用鉄供給剤の使用方法も特に 限定されない。例えば、土と混合 (粉体状で、塊状で)する、土に散布 (粉体状で)す る、土中に埋める (粉体状で、塊状で)等の使用方法が挙げられる。 [0035] There are no particular limitations on the method of using this other iron supply agent for plants using a biodegradable extender as a matrix. For example, it can be mixed with the soil (in powder form or in a lump form), sprayed on the soil (in powder form), or embedded in the soil (in powder form or lump form).
[0036] [4]アルカリ土壌用植物用鉄供給剤の製造方法 [0036] [4] Method for producing plant iron supply agent for alkaline soil
(1)本発明のアルカリ土壌用植物用鉄供給剤の製造方法 (1) Production method of plant iron supply agent for alkaline soil of the present invention
本発明の製造方法は、前述のように特に限定されず種々の方法を用いることができ るが、例えば、ァスコルビン酸粉末と、鉄成分粉末と、水と、を含有する混合物を加熱 して、ァスコルビン酸及び鉄成分が溶解されて得られた水溶液を得る溶解工程を備 えることができる。 The production method of the present invention is not particularly limited as described above, and various methods can be used. For example, by heating a mixture containing ascorbic acid powder, iron component powder, and water, A dissolution step for obtaining an aqueous solution obtained by dissolving ascorbic acid and an iron component can be provided.
[0037] 上記「ァスコルビン酸粉末」は、上記ァスコルビン酸を主成分 (通常、純度 99%以上 )とする粉末であり、その純度は特に限定されない。また、粉末形態であるとき、その 粒子形状等は特に限定されない。 [0037] The "ascorbic acid powder" is a powder containing ascorbic acid as a main component (usually having a purity of 99% or more), and the purity is not particularly limited. Moreover, when it is a powder form, the particle shape etc. are not specifically limited.
[0038] 上記「鉄成分粉末」は、前記の各種の鉄成分を主成分とする粉末である。この鉄成 分粉末としては FeO粉末が好ましい。鉄成分粉末が FeO粉末である場合、この FeO 粉末に含有される FeOの量は特に限定されないが、通常、 FeO粉末全体に対して F eOが 50質量%以上 (好ましくは 65質量%以上、 100質量%であってもよい)である。 この FeO粉末はどのような FeO粉末を用いてもよぐ後述する FeO粉末 (鉄分を含有 するダスト(以下、「ダスト」ということもある。)を造粒してなる造粒品、及び Z又はこの ダストと還元剤とを造粒してなる造粒品、を真空加熱したのち真空急冷して得られた FeO粉末)、及び各種市販の FeO粉末を用いることができる。これらのなかでは、上 記造粒品を真空加熱したのち真空急冷して得られた FeO粉末が好ましい。 The “iron component powder” is a powder mainly composed of the various iron components. This iron component powder is preferably FeO powder. When the iron component powder is FeO powder, the amount of FeO contained in the FeO powder is not particularly limited, but usually FeO is 50 mass% or more (preferably 65 mass% or more, preferably 100 mass% or more based on the entire FeO powder). It may be mass%). This FeO powder can be any type of FeO powder. The FeO powder described later (a granulated product obtained by granulating iron-containing dust (hereinafter sometimes referred to as “dust”), and Z or A granulated product obtained by granulating this dust and a reducing agent, FeO powder obtained by vacuum heating and vacuum quenching), and various commercially available FeO powders can be used. Among these, FeO powder obtained by heating the granulated product in a vacuum and then quenching in a vacuum is preferable.
上記「水」は、前述のごとくどのような水も用いることができる。 As the “water”, any water can be used as described above.
[0039] 上記「混合物」におけるァスコルビン酸粉末と FeO粉末等の鉄成分粉末と水との仕 込み量は特に限定されないが、ァスコルビン酸粉末 (純度 100%と仮定):鉄成分粉 末 (純度 100%と仮定):水(純度 100%と仮定)の質量比で、 60〜90 : 7〜28 : 3〜2 0の割合で用いることが好ましぐ 65〜85 : 10〜24 : 5〜17. 5の割合で用いることが より好ましぐ 68〜72: 10〜22: 10〜15の割合で用いることが特に好ましい。 [0039] The amount of ascorbic acid powder and iron component powder such as FeO powder and water charged in the above "mixture" is not particularly limited, but ascorbic acid powder (assuming purity 100%): iron component powder (purity 100 (Assuming%): The mass ratio of water (assuming purity of 100%) is preferably 60-90: 7-28: 3-20, 65-85: 10-24: 5-17 Use at a rate of 5 It is particularly preferable to use it at a ratio of 68-72: 10-22: 10-15.
[0040] 上記混合物には、ァスコルビン酸粉末、鉄成分粉末及び水以外に他の成分が含有 されていてもよぐ含有されていなくてもよい。他の成分を含有する場合は、水に溶解 した状態で含有されてもよぐ水に溶解されない状態で含有されてもよい。他の成分 としては、例えば、メタノール及びエタノールが挙げられる。これらを含有させることで 減圧環境下においても水をよりスムーズに除去することができる。これらは 1種のみが 含有されていてもよぐ 2種以上が含有されていてもよい。 [0040] The above mixture may or may not contain other components besides ascorbic acid powder, iron component powder and water. When other components are contained, they may be contained in a state dissolved in water or in a state not dissolved in water. Examples of other components include methanol and ethanol. By containing these, water can be removed more smoothly even under a reduced pressure environment. These may contain only one kind or two or more kinds.
[0041] 上記「加熱」における加熱条件は特に限定されないが、加熱温度は 120°C以下に 保持することが好ましい。 120°Cを超えると Fe3+イオン濃度が高くなる傾向にあるから である。この加熱による水溶液の温度は、 110°C以下がより好ましぐ 105°C以下が 更に好ましぐ 100°C以下が特に好ましい。一方、下限温度は特に限定されず、例え ば、 40°C以上が好ましぐ 50°C以上がより好ましぐ 60°C以上が特に好ましい。これ らの加熱の際の上限温度及び下限温度は各々組合せとすることができる。即ち、例 えば、 40〜120°Cが好ましぐ 50〜110°Cがより好ましぐ 60〜100°Cが更に好まし い。これら以外の組合せであってもよい。尚、加熱の際の圧力条件は特に限定されな い。 [0041] The heating conditions in the above "heating" are not particularly limited, but the heating temperature is preferably maintained at 120 ° C or lower. This is because the Fe 3+ ion concentration tends to increase above 120 ° C. The temperature of the aqueous solution by this heating is more preferably 110 ° C. or less, more preferably 105 ° C. or less, and further preferably 100 ° C. or less. On the other hand, the lower limit temperature is not particularly limited. For example, 40 ° C or higher is preferable, 50 ° C or higher is more preferable, and 60 ° C or higher is particularly preferable. The upper limit temperature and the lower limit temperature at the time of heating can be combined. That is, for example, 40 to 120 ° C is preferable, and 50 to 110 ° C is more preferable, and 60 to 100 ° C is more preferable. Combinations other than these may be used. The pressure conditions for heating are not particularly limited.
この加熱により、ァスコルビン酸がより多く水に溶解され、これに従い FeO等の鉄成 分の溶解量も増え、目的とする Fe2+イオン又は Fe2+イオン錯体の濃度が高くなるも のと考えられる。 This heating is dissolved in more water Asukorubin acid, which in accordance with the amount of dissolved TetsuNaru components such as FeO even more, even Noto consider the concentration of Fe 2+ ions or Fe 2+ ion complex of interest is higher It is done.
[0042] 本発明の製造方法では、上記溶解工程の後に水不溶性成分を除去する工程を備 えることができる。この水不溶性成分としては、溶解しきらないァスコルビン酸粉末及 び溶解しきらない鉄成分粉末等が挙げられる。除去方法は特に限定されないが、通 常、濾過により行うことができる。即ち、濾過工程を備えることができる。この際の濾過 条件は特に限定されないが、例えば、濾過フィルターには孔径 10 m以下 (より好ま しくは 5 μ m以下、更に好ましくは 3 μ m以下)のメンブランフィルターを用いることが 好ましい。 [0042] The production method of the present invention can include a step of removing the water-insoluble component after the dissolution step. Examples of the water-insoluble component include ascorbic acid powder that cannot be dissolved and iron component powder that cannot be dissolved. The removal method is not particularly limited, but can usually be performed by filtration. That is, a filtration step can be provided. The filtration conditions at this time are not particularly limited. For example, it is preferable to use a membrane filter having a pore size of 10 m or less (more preferably 5 μm or less, more preferably 3 μm or less) as the filtration filter.
[0043] また、本他の植物用鉄供給剤を得る場合は、上記溶解工程の後に、又は上記溶解 工程及び上記濾過工程の後に、更に、上記水溶液力ゝら水を除去する乾燥工程を備 えることができる。この乾燥工程における乾燥条件は特に限定されず、自然乾燥をさ せてもよいが、前述した除去方法及び乾燥条件を用いることが好ましい。即ち、減圧 加熱により水を除去することが好ましい。加熱し、且つ水分を徐々に減ずることで、水 溶性であり、且つ抗酸ィ匕性に優れた Fe2+イオン成分 (Fe2+錯体等)が濃縮され、本 他の植物用鉄供給剤が得られるものと考えられる。 [0043] Further, when obtaining the other iron supply agent for plants, a drying step for removing water from the aqueous solution is further provided after the dissolution step or after the dissolution step and the filtration step. I can. The drying conditions in this drying step are not particularly limited, and natural drying may be performed, but it is preferable to use the above-described removal method and drying conditions. That is, it is preferable to remove water by heating under reduced pressure. By heating and gradually reducing the water content, Fe 2+ ion components (Fe 2+ complex, etc.) that are water-soluble and have excellent acid-fast properties are concentrated, and other plant iron suppliers Is considered to be obtained.
[0044] 更に、前記本他の植物用鉄供給剤を得る際には、更に、精製工程を備えることもで きる。精製工程は、水溶性成分を精製する工程である。即ち、例えば、上記水溶液か ら水を除去して得られる植物用鉄供給剤を水と接触させて溶解可能部分を溶解させ た後、上記と同様にして水不溶性成分を除去して抽出する抽出工程と、この抽出ェ 程で得られた抽出水溶液力ゝら水を除去する再乾燥工程と、を備えることができる。 [0044] Further, when obtaining the other iron supply agent for plants, a purification step may be further provided. The purification process is a process for purifying water-soluble components. That is, for example, extraction is performed by removing the water-insoluble components in the same manner as described above after contacting the iron supply agent for plants obtained by removing water from the aqueous solution with water to dissolve the soluble portion. A step and a re-drying step for removing water from the extraction aqueous solution obtained in this extraction step.
[0045] (2)生分解性増量剤をマトリックスとする本更に他の本発明のアルカリ土壌用植物用 鉄供給剤の製造方法 [0045] (2) A method for producing an iron supply agent for an alkaline soil plant according to the present invention, wherein the biodegradable extender is used as a matrix.
生分解性増量剤をマトリックスとする本更に他の植物用鉄供給剤の製造方法は特 に限定されないが、例えば、撥水性を有する生分解性増量剤 (通常、粉体又は粒体 である。)である泥炭及び Z又は粘土と、ァスコルビン酸粉末と、鉄成分粉末とを混合 し、造粒して得ることができる。 There are no particular limitations on the method for producing the other iron supply agent for plants using the biodegradable extender as a matrix. For example, biodegradable extenders having water repellency (usually powder or granules). ) Peat and Z or clay, ascorbic acid powder, and iron component powder are mixed and granulated.
混合の方法は特に限定されず、モルタルミキサ及びォムニミキサ等を用いたドライ ブレンドでもよぐニーダー及びウエットパン等により混合してもよい。更に、造粒の方 法も特に限定されないが、通常、押出成形法により造粒される。また、押出成形により 混合と造粒とを連続して行えば、工程が簡略ィ匕でき好ましい。このドライブレンド及び 押出成形等の温度は特に限定されず、室温 (例えば、 15〜35°C)でもよぐ必要に 応じて 40〜90°C程度に加熱してもよ!/、。 The mixing method is not particularly limited, and it may be mixed by a dry kneader using a mortar mixer, an omni mixer or the like, or a kneader or a wet pan. Furthermore, the granulation method is not particularly limited, but it is usually granulated by an extrusion method. Further, it is preferable that mixing and granulation are continuously performed by extrusion molding because the process can be simplified. The temperature of the dry blending and extrusion molding is not particularly limited, and it may be room temperature (for example, 15 to 35 ° C) or may be heated to about 40 to 90 ° C if necessary! /.
このァスコルビン酸粉末及び鉄成分粉末については、上記(1)本発明の植物用鉄 供給剤の製造方法における各々の記載をそのまま適用できる。但し、泥炭及び/又 は粘土、ァスコルビン酸粉末及び鉄成分粉末として配合された FeO粉末の合計を 10 0質量%とした場合に、ァスコルビン酸粉末は 1〜30質量%、 FeO粉末は 1〜30質 量%配合される。 About this ascorbic acid powder and iron component powder, each description in the manufacturing method of the above-mentioned (1) iron supply agent for plants of this invention is applicable as it is. However, when the total of FeO powder blended as peat and / or clay, ascorbic acid powder and iron component powder is 100 mass%, ascorbic acid powder is 1-30 mass%, FeO powder is 1-30 mass%. It is blended in mass%.
本更に他の植物用鉄供給剤は、泥炭及び Z又は粘土と、前記本他の植物用鉄供 給剤とを混合し、造粒して得ることもできる。このときの混合及び造粒は上記と同様に して行うことができる。 Still other plant iron supplies include peat and Z or clay and the other plant iron supplies. It can also be obtained by mixing with a feed agent and granulating. The mixing and granulation at this time can be performed in the same manner as described above.
また、前記本他の植物用鉄供給剤を用いる場合、泥炭及び/又は粘土と、ァスコル ビン酸粉末と、 FeO粉末との質量割合は上記と同様であり、この質量割合は、本他の 植物用鉄供給剤を製造する際に用いるァスコルビン酸粉末及び FeO粉末の各々の 質量割合、並びに泥炭及び/又は粘土と、本他の植物用鉄供給剤との質量割合によ つて調整することができる。 In addition, when the above-mentioned other iron supply agent for plants is used, the mass proportions of peat and / or clay, ascorbic acid powder, and FeO powder are the same as above, and this mass proportion is the same as that of other plants. It can be adjusted according to the mass ratio of ascorbic acid powder and FeO powder used in the production of iron supplements and the mass ratio of peat and / or clay and other iron supplements for plants. .
[0046] (3) FeO粉末の製造方法 [0046] (3) Method for producing FeO powder
本発明の製造方法及び他の本発明の製造方法で、鉄成分粉末として特に FeO粉 末を用いる場合、この FeO粉末は、鉄分を含有するダストを造粒してなる造粒品、及 び Z又はこのダストと還元剤とを造粒してなる造粒品、を真空加熱したのち真空急冷 して得られた FeO粉末であることが好まし 、。 When FeO powder is used as the iron component powder in the production method of the present invention and other production methods of the present invention, this FeO powder is a granulated product obtained by granulating dust containing iron, and Z Or, it is preferable to use a FeO powder obtained by vacuum-cooling a granulated product obtained by granulating this dust and a reducing agent.
[0047] この FeO粉末は、 FeO以外にも、通常、 CaAl O、 FeAl O、 CaFe Si O、 CaSi [0047] In addition to FeO, this FeO powder is usually CaAl O, FeAl O, CaFe Si O, CaSi.
2 4 2 4 2 2 6 2 4 2 4 2 2 6
O及び MgFe Oのうちの少なくとも 1種の複酸化物を含有する。これらの複酸化物Contains at least one double oxide of O and MgFe 2 O. These double oxides
2 5 2 4 2 5 2 4
は 1種のみが含有されてもよぐ 2種以上が含有されてもよい。また、複酸化物の含有 量は、 FeO粉末全体を 100質量%とした場合に 0. 5〜10質量%が好ましい。この範 囲であれば抗酸ィ匕性に特に優れた鉄供給剤を得ることができる。 May contain only one kind or two or more kinds. The content of the double oxide is preferably 0.5 to 10% by mass when the entire FeO powder is 100% by mass. Within this range, it is possible to obtain an iron supplier that is particularly excellent in acid resistance.
更に、この FeO粉末を構成する粒子の粒子径は特に限定されないが、例えば、粒 径力 000 μ m以下であり、多種の粒径の粉末が混在した FeO粉末であればよい。 更には、多孔性の粒子が含まれていてもよい。 Further, the particle diameter of the particles constituting the FeO powder is not particularly limited, but may be any FeO powder having a particle diameter force of 000 μm or less and a mixture of powders having various particle diameters. Furthermore, porous particles may be included.
[0048] 上記「鉄分を含有するダスト」は鉄分を含有するもの (集塵粉等)である。この鉄分と しては、酸化鉄、その他の鉄化合物及び金属鉄が挙げられる。これらは 1種のみが含 有されてもよぐ 2種以上が含有されてもよい。このダストに含有される鉄分量は特に 限定されないが、通常、ダスト全体を 100質量%とした場合に金属鉄換算で 30質量 %以上(より好ましくは 35〜90質量%、更に好ましくは 40〜80質量%)である。また 、ダストには、鉄分以外にも他の成分が含有されてもよい。他の成分としては Zn、 Ni 、 Cu及び Mn等が挙げられる。これらは単体金属でもよぐ酸化物等の化合物でもよ い。更に、これらは 1種のみが含有されてもよぐ 2種以上が含有されてもよい。 鉄分を含有するダストの形状は特に限定されず、小片又は粉体と小片との混合物 等であってもよいが、通常、粉体である。この粉体の平均粒径は特に限定されないが[0048] The "dust containing iron" is one containing iron (dust collection powder or the like). Examples of the iron component include iron oxide, other iron compounds, and metallic iron. These may contain only one kind or two or more kinds. The amount of iron contained in the dust is not particularly limited, but usually 30% by mass or more (more preferably 35 to 90% by mass, still more preferably 40 to 80% in terms of metallic iron when the total dust is 100% by mass. Mass%). Further, the dust may contain other components besides iron. Other components include Zn, Ni, Cu and Mn. These may be simple metals or compounds such as oxides. Furthermore, these may contain only 1 type, and may contain 2 or more types. The shape of the dust containing iron is not particularly limited, and may be small pieces or a mixture of powder and small pieces, but is usually powder. The average particle size of this powder is not particularly limited
3〜: LO /z mが好ましい。 3 to: LO / z m is preferable.
[0049] この鉄分を含有するダストとしては、鍛造工程で発生する鍛造ショット集塵粉、及び 製鋼工程で発生する電気炉ダスト、高炉ダスト、転炉ダスト、キュポラダスト等の製鋼 ダストが挙げられる。これらは 1種のみを用いてもよぐ 2種以上を併用してもよい。特 に塩素分を予め水洗除去(一部又は全部)したダストが好ましい。特にダストに含有さ れる塩素分は 0. 5質量%以下(より好ましくは 0. 4質量%以下、更に好ましくは 0. 3 質量%以下)が好ましい。 [0049] Examples of the dust containing iron include forged shot dust collected in the forging process and steelmaking dust such as electric furnace dust, blast furnace dust, converter dust, and cupola dust generated in the steel making process. These may be used alone or in combination of two or more. In particular, dust from which the chlorine content has been removed by washing with water (partially or entirely) is preferred. In particular, the chlorine content in the dust is preferably 0.5% by mass or less (more preferably 0.4% by mass or less, and still more preferably 0.3% by mass or less).
[0050] 上記「造粒品」は、鉄分を含有するダスト、又はこのダストと還元剤とを含有する。造 粒により、真空加熱の際に Fe O、 Fe O及び Fe (単体)から FeOへの還元又は酸 [0050] The above "granulated product" contains iron-containing dust or the dust and a reducing agent. Granulation reduces or converts Fe O, Fe 2 O and Fe (single) to FeO or acid during vacuum heating
2 3 3 4 2 3 3 4
化が促進される。 Is promoted.
造粒品を構成する粒子の形状は特に限定されず、球体、楕円体、半球体、立方体 、直方体、円柱体及びプリケット等のいずれでもよい。更に、造粒品は緻密体でもよく 、多孔質体であってもよい。またその粒径 (球形であるときは直径、その他の形状であ るときは最短寸法)は 25mm以下(より好ましくは 15mm以下、更に好ましくは 10mm 以下、通常 3mm以上)が好ましい。 The shape of the particles constituting the granulated product is not particularly limited, and may be any of a sphere, an ellipsoid, a hemisphere, a cube, a cuboid, a cylinder, a plecket, and the like. Further, the granulated product may be a dense body or a porous body. Further, the particle size (diameter in the case of a sphere, shortest dimension in the case of other shapes) is preferably 25 mm or less (more preferably 15 mm or less, further preferably 10 mm or less, usually 3 mm or more).
[0051] 上記「還元剤」は、 2価以上に酸化された鉄化合物を還元する成分である。還元剤 としては、金属鉄、その混合物、カーボン、その混合物等を用いることができる。特に 、鉄切削屑、鉄研磨屑、鉄粉、銑鉄及び鋼等に用いられる還元剤、各種廃材 (タイヤ 屑、木材廃材等)等が好ましい。これらは 1種のみを用いてもよぐ 2種以上を併用し てもよい。 [0051] The "reducing agent" is a component that reduces an iron compound that has been oxidized to a valence of 2 or more. As the reducing agent, metallic iron, a mixture thereof, carbon, a mixture thereof, or the like can be used. In particular, reducing agents used for iron cutting scraps, iron polishing scraps, iron powder, pig iron and steel, various waste materials (tire scraps, wood waste materials, etc.) and the like are preferable. These may be used alone or in combination of two or more.
還元剤の形状は特に限定されな 、が、ダストとの接触面積が大き 、ことが好ま ヽ ため粉末、顆粒及び小片等が好ましぐ特に粉末が好ましい。更に平均粒径は 200 m以下 (好ましくは 180 μ m以下)が好ま U、。 The shape of the reducing agent is not particularly limited, but it is preferable that the contact area with the dust is large, so that powder, granules, small pieces, etc. are particularly preferable. Furthermore, the average particle size is preferably 200 m or less (preferably 180 μm or less).
造粒品中の還元剤の含有量は特に限定されないが、ダストを 100質量部とした場 合に 100質量部以下 (より好ましくは 90質量部以下、更に好ましくは 80質量部以下、 通常 30質量部以上)が好ま 、。 [0052] また、造粒品には、通常、ノインダが含有される。バインダの種類は特に限定され ないが、アルミナセメントが好ましい。その配合量は、鉄分を含有するダスト、又はこの ダストと還元剤との合計を 100質量部とした場合に 3〜20質量部(より好ましくは 3〜 15質量部、更に好ましくは 3〜12質量部)であることが好ましい。この範囲では、造粒 をスムーズに行うことができ、造粒品の脆化も抑制できる。 The content of the reducing agent in the granulated product is not particularly limited, but when the dust is 100 parts by mass, it is 100 parts by mass or less (more preferably 90 parts by mass or less, more preferably 80 parts by mass or less, usually 30 parts by mass). More than part). [0052] Further, the granulated product usually contains noinda. The type of binder is not particularly limited, but alumina cement is preferable. The blending amount is 3 to 20 parts by mass (more preferably 3 to 15 parts by mass, further preferably 3 to 12 parts by mass) when the dust containing iron content or the total of the dust and the reducing agent is 100 parts by mass. Part). In this range, granulation can be performed smoothly and embrittlement of the granulated product can be suppressed.
[0053] 上記「真空加熱」を行うことで FeO粉末中の FeO濃度を高くすることができる。この 真空加熱を行う際の真空度は特に限定されないが 0. 1〜13. 3kPa (より好ましくは 2 . 6-13. 3kPa、特に好ましくは 4. 0〜6. 7kPa)が好ましい。この範囲では金属鉄 の残留や FeOが Fe O等へ酸ィ匕されることを効果的に抑制できる。尚、この真空雰 [0053] By performing the "vacuum heating", the FeO concentration in the FeO powder can be increased. The degree of vacuum during this vacuum heating is not particularly limited, but is preferably 0.1 to 13.3 kPa (more preferably 2.6-13. 3 kPa, particularly preferably 4.0 to 6.7 kPa). Within this range, it is possible to effectively suppress residual metallic iron and oxidation of FeO to Fe 2 O and the like. This vacuum atmosphere
3 4 3 4
囲気における酸素分圧と同等の酸素分圧の不活性ガス雰囲気下で、真空加熱に変 えて同様に加熱することで同様に FeO濃度の高い FeO粉末を得ることができる。 In an inert gas atmosphere with an oxygen partial pressure equivalent to the oxygen partial pressure in the atmosphere, it is possible to obtain a FeO powder with a high FeO concentration by heating in the same manner instead of vacuum heating.
[0054] 真空加熱を行う際の加熱温度 (造粒品自体を測定した測定値)は 600〜1100°C ( より好ましくは 800〜950°C)が好ましい。但し、造粒品が還元剤を含有する場合は 8 00°C以上とすることが好ましい。この範囲では、 FeO含有量が特に高い FeO粉末が 得られ、加熱過程で鉄分を含有するダストが溶融することも防止できる。 [0054] The heating temperature (measured value obtained by measuring the granulated product itself) during vacuum heating is preferably 600 to 1100 ° C (more preferably 800 to 950 ° C). However, when the granulated product contains a reducing agent, it is preferably 800 ° C or higher. In this range, FeO powder having a particularly high FeO content can be obtained, and it is possible to prevent melting of iron-containing dust during the heating process.
また、加熱時間は特に限定されないが 30分以上 (より好ましくは 30分以上、且つ 6 時間以内)が好ましい。 The heating time is not particularly limited, but is preferably 30 minutes or longer (more preferably 30 minutes or longer and within 6 hours).
尚、ダストに酸化亜鉛等が含有される場合は、還元されて金属亜鉛となり、 600°C 以上、且つ 1. 56kPa程度の真空下で蒸発して回収できる。これにより FeOの純度を 更に向上させることができる。 When zinc oxide or the like is contained in the dust, it is reduced to metal zinc, which can be recovered by evaporation under a vacuum of 600 ° C or higher and about 1.556 kPa. This can further improve the purity of FeO.
[0055] 造粒品の加熱は、通常、熱処理炉を用いてなされる。この熱処理炉は、少なくともヒ ータを備え、投入される造粒品を均一に加熱できるものであれば、特に限定されない 。熱処理炉としては、例えば、ローラーハース炉及びロータリーキルン等が挙げられ る。造粒品は、熱処理炉内を移動しながら、例えば、攪拌翼を備える攪拌手段等によ り粉末化される。この熱処理炉は、還元によって生成した金属亜鉛等を回収するため の回収器を備えて 、てもよ 、。熱処理炉への造粒品の投入量は特に限定されな ヽ 1S 熱処理炉で加熱される造粒品全体への熱伝導を考慮し、炉床に散布された造粒 品の平均高さが、通常、 100mm以下、特に 80mm以下、更に 30mm以下となる投 入量であることが好ましい。 [0055] The granulated product is usually heated using a heat treatment furnace. The heat treatment furnace is not particularly limited as long as it includes at least a heater and can uniformly heat the granulated product to be charged. Examples of the heat treatment furnace include a roller hearth furnace and a rotary kiln. The granulated product is powdered by, for example, a stirring means equipped with a stirring blade while moving in the heat treatment furnace. This heat treatment furnace may be equipped with a recovery device for recovering metallic zinc and the like produced by the reduction. The amount of granulated product input to the heat treatment furnace is not particularly limited し Considering heat conduction to the entire granulated product heated in the 1S heat treatment furnace, the average height of the granulated product sprayed on the hearth is Usually, it is 100mm or less, especially 80mm or less, and 30mm or less. It is preferable that it is an amount.
[0056] 上記「真空急冷」により真空加熱で生成された高温の FeO粉末を酸化させることな く冷却できる。この真空急冷の際の真空度は特に限定されないが 13. 3kPa以下 (よ り好ましくは 6. 7kPa以下、通常 5. 3kPa以上)が好ましい。また、降温速度は特に限 定されないが 5〜150°CZ分とすることが好ましい。この真空急冷では 300°C以下(よ り好ましくは 200°C以下、特に好ましくは 150°C以下)に冷却することが好ましい。 [0056] By the above "vacuum quenching", the high-temperature FeO powder produced by vacuum heating can be cooled without being oxidized. The degree of vacuum during this vacuum quenching is not particularly limited, but is preferably 13.3 kPa or less (more preferably 6.7 kPa or less, usually 5.3 kPa or more). The temperature drop rate is not particularly limited, but is preferably 5 to 150 ° CZ. In this vacuum quenching, it is preferable to cool to 300 ° C or lower (more preferably 200 ° C or lower, particularly preferably 150 ° C or lower).
[0057] 特に FeO含有量のより多い FeO粉末を得る目的においては、金属鉄を含有する造 粒品を用いることが好ましい。金属鉄の含有量は、造粒品に含有される鉄分の全量 を 100質量%とした場合に 5質量%以上 (より好ましくは 5〜85質量%、更に好ましく は 8〜50質量%)が好ましい。この造粒品を用いた場合には、例えば、鉄分全量に 対する FeOの含有量が 80質量%以上(更には 85質量%以上、特に 90質量%以上 )の FeO粉末を得ることができる。 [0057] In particular, for the purpose of obtaining FeO powder having a higher FeO content, it is preferable to use a granulated product containing metallic iron. The content of metallic iron is preferably 5% by mass or more (more preferably 5 to 85% by mass, still more preferably 8 to 50% by mass) when the total amount of iron contained in the granulated product is 100% by mass. . When this granulated product is used, for example, an FeO powder having a FeO content of 80 mass% or more (more preferably 85 mass% or more, particularly 90 mass% or more) based on the total iron content can be obtained.
[0058] 上記のような金属鉄を含有する造粒品を構成する鉄分を含有するダスト [下記(1) 及び(5) ]及びこのダストと還元剤との組合せ [下記(2)、(3)及び (4) ]としては(1) 鍛造ショット集塵粉のみ、(2)鍛造ショット集塵粉と金属鉄 (鉄粉等)との混合物、 (3) 電気炉ダストと金属鉄 (鉄粉等)との混合物、(4)高炉ダストと金属鉄 (鉄粉等)との混 合物、(5)転炉ダストのみ、等が挙げられる。これらは 1種のみを用いてもよぐ 2種以 上併用してもよい。 [0058] Dust containing iron that constitutes a granulated product containing metallic iron as described above [(1) and (5)] and a combination of this dust and a reducing agent [(2), (3 ) And (4)]: (1) Forged shot dust collection powder only, (2) Mixture of forged shot dust collection powder and metal iron (iron powder, etc.), (3) Electric furnace dust and metal iron (iron powder) Etc.), (4) mixture of blast furnace dust and metallic iron (iron powder, etc.), and (5) converter dust only. These may be used alone or in combination of two or more.
実施例 Example
[0059] 以下、本発明を実施例により具体的に説明する。 [0059] The present invention will be specifically described below with reference to examples.
[l]FeO粉末の製造 [l] Manufacture of FeO powder
Fe80質量0 /0 (以下、%と略記する。)、 ZnO. 02%、 CaO. 01%、 MnO. 06%及び SiO. 06%等が含有され、平均粒径が 100 mの鍛造ショット集塵粉 82%と、平均粒 径が 75 mの鉄粉 10%と、アルミナセメント 5%と、ベントナイト 3%とを用いて直径 8 mm且つ長さ約 20mmの円柱形に造粒した。得られた造粒品を真空加熱槽 (ローラ 一ハース炉)により 800°Cで 30分間、次いで 850°Cで 30分間、その後、 900°Cで 1時 間、各々真空加熱した。 Fe80 mass 0/0 (hereinafter,% abbreviated.), ZnO. 02%, CaO. 01%, MnO. 06% and SiO. 06% or the like is contained, forging shot dust collecting an average particle diameter of 100 m It was granulated into a cylindrical shape having a diameter of 8 mm and a length of about 20 mm using 82% of powder, 10% of iron powder having an average particle diameter of 75 m, 5% of alumina cement, and 3% of bentonite. The obtained granulated product was heated in a vacuum heating tank (roller and hearth furnace) at 800 ° C. for 30 minutes, then at 850 ° C. for 30 minutes, and then at 900 ° C. for 1 hour.
次いで、真空急冷槽で降温速度 20°CZ分で 400°Cまで真空急冷し、更に、真空 冷却槽内の雰囲気を窒素置換して、更に降温速度 13°CZ分で 200°Cまで冷却し、 その後、室温にまで降温させて FeO粉末を得た。 Next, vacuum quenching is performed in a vacuum quenching bath to 400 ° C at a temperature drop rate of 20 ° CZ, and further vacuum The atmosphere in the cooling tank was replaced with nitrogen, and further cooled to 200 ° C at a rate of temperature decrease of 13 ° CZ, and then cooled to room temperature to obtain FeO powder.
この FeO粉末に含有される FeOを、試薬 FeO粉末とシリコン粉末とを所定割合で混 合してなる混合粉末を用いて X線回折法により予め作成した検量線により定量したと ころ、含有量は 90質量%であった。 When FeO contained in this FeO powder was quantified by a calibration curve prepared in advance by X-ray diffraction using a mixed powder obtained by mixing a reagent FeO powder and silicon powder at a predetermined ratio, the content was It was 90% by mass.
[0060] [2]ァスコルビン酸鉄水溶液における Fe2+イオンの安定性 [0060] [2] Stability of Fe 2+ ions in iron ascorbate aqueous solution
実験例 1〜3 Experimental example 1-3
(1)ァスコルビン酸鉄水溶液の pHと Fe2+イオン濃度の相関 (1) Correlation between pH of iron ascorbate aqueous solution and Fe 2+ ion concentration
500ミリリットルの蒸留水に 2. 5gのァスコルビン酸を溶解させ、ァスコルビン酸水溶 液を作製した。その後、この水溶液に上記 [1]で製造した FeO粉末を 1. Og投入し、 30分間攪拌し、次いで、濾過し、挟雑物を除いた。その後、濾過後の水溶液から 20 ミリリットルづっ分取し、それぞれ 5個の容器に投入し、これらのうちの 4個の容器中の 水溶液の ρΗを水酸ィ匕ナトリウム水溶液により、各々 7. 0、 8. 0及び 9. 0に調整した。 尚、 pH調整をしていないァスコルビン酸水溶液の pHは 3. 4であった。 An aqueous solution of ascorbic acid was prepared by dissolving 2.5 g of ascorbic acid in 500 ml of distilled water. Thereafter, 1. Og of the FeO powder produced in [1] above was added to this aqueous solution, stirred for 30 minutes, and then filtered to remove impurities. Thereafter, 20 milliliters are taken from the aqueous solution after filtration and put into 5 containers, and ρΗ of the aqueous solution in 4 of these containers is 7.0, respectively, with sodium hydroxide aqueous solution. Adjusted to 8.0 and 9.0. The pH of the ascorbic acid aqueous solution not adjusted for pH was 3.4.
[0061] 上記のようにして調製したそれぞれ pHの異なる 3種類のァスコルビン酸水溶液に ついて、水溶液調製時、又は pH調整時、並びに 24時間、 48時間及び 120時間経 過後の各々の Fe2+イオン濃度を測定した。併せてそれぞれの水溶液の pHも測定し た。 Fe2+イオン濃度 ίお IS K0102に基づくフエナント口リン吸光光度法により測定し た。尚、この測定では常に直射日光の差し込まない室内において作業を行った。結 果を表 1に記載する。 [0061] For three types of ascorbic acid aqueous solutions having different pH values prepared as described above, each Fe 2+ ion at the time of aqueous solution preparation or pH adjustment, and after 24 hours, 48 hours, and 120 hours, respectively. Concentration was measured. In addition, the pH of each aqueous solution was also measured. The Fe 2+ ion concentration was measured by a phenantorin phosphorus absorptiometry based on IS K0102. In this measurement, the work was always performed in a room where direct sunlight was not inserted. The results are listed in Table 1.
[0062] [表 1] [0062] [Table 1]
表 1の結果によれば、実験例 1 3のいずれにおいても経時とともに pHが低下する 傾向にあり、 Fe2+イオン濃度が高濃度に保たれていることが分かる。ァスコルビン酸 はアルカリ条件下で酸ィ匕されてデヒドロアスコルビン酸となる力 これによつて水溶液 の pHが低下したものと考えられ、 pHの低下によって FeOの溶解性が高くなり、より多 くの FeOが水に溶解し、且つ還元性を有するァスコルビン酸により Fe2+の Fe3+への 酸化が抑えられ、これらの相乗効果によって初期の pHの高 、場合であっても Fe2+ィ オン濃度が高濃度に保たれるものと考えられる。 According to the results in Table 1, it can be seen that in all of Experimental Examples 13 and 3, the pH tends to decrease with time, and the Fe 2+ ion concentration is maintained at a high concentration. Ascorbic acid is acidified under alkaline conditions to form dehydroascorbic acid. The pH of the FeO solution is considered to have decreased, and the solubility of FeO increases as the pH decreases, so that more FeO dissolves in water and reductive ascorbic acid converts Fe 2+ to Fe 3+ . Oxidation is suppressed, and these synergistic effects are considered to maintain the Fe 2+ ion concentration at a high concentration even when the initial pH is high.
[0064] (2)上記(1)において 120時間経過後の水溶液の pHを調整した場合の Fe2+イオン 濃度 [0064] (2) Fe 2+ ion concentration when adjusting pH of aqueous solution after 120 hours in (1) above
実験例 4〜6 Experimental examples 4-6
上記(1)における初期 pHの異なる 3種類の水溶液について、各々 120時間経過後 、低下した pHを水酸ィ匕ナトリウム水溶液により初期 pHに近似の値となるように調整し 、それぞれの Fe2+イオン濃度を測定した。また、 pH調整した各々の水溶液の pHが 2 4時間には再び低下したため、水酸ィ匕ナトリウム水溶液により再度 pHを初期 pHに近 似の値に調整し、それぞれの Fe2+イオン濃度を測定した。この pH調整とそれぞれの Fe2+イオン濃度の測定とを 3回繰り返した。結果を表 2に記載する。 For each of the three types of aqueous solutions with different initial pH values in (1) above, after 120 hours each, the lowered pH was adjusted to an approximate value for the initial pH with aqueous sodium hydroxide solution, and each Fe 2+ The ion concentration was measured. In addition, since the pH of each aqueous solution adjusted for pH decreased again in 24 hours, the pH was adjusted again to a value close to the initial pH with sodium hydroxide aqueous solution, and the respective Fe 2+ ion concentrations were measured. did. This pH adjustment and measurement of each Fe 2+ ion concentration were repeated three times. The results are listed in Table 2.
[0065] [表 2] [0065] [Table 2]
α α
整整整調調調回目回目回目 H 3 H 2 H 1 p t— 222+++濃度濃度濃度イオイオイオ Fン Fン Fンeee Adjusting Adjusting Adjusting Time 1st Time H 3 H 2 H 1 pt— 2 22 +++ Concentration Concentration Concentration Concentration Concentration Concentration Concentration
()/リト/Jト/ト!))ルルル、ッッッmgmgmg () / Lito / J To / To!)) Rururu, tsutsu mgmgmg
/ εοios6 ,~o ' * / εοios6, ~ o '*
X X
a a
実験例 4 6の pH調整 1 2回目の pH及び Fe イオン濃度の各々の値は、 pH調 整時の値 (初期値) ZpH調整力も 24時間経過後の値、である。また、 pH調整 3回目 では、初期値のみを測定した。 Example 4 of pH adjustment in 6 1 Each value of pH and Fe ion concentration in the second time is the value at the time of pH adjustment (initial value), and the value of ZpH adjustment power is also a value after 24 hours. In the third pH adjustment, only the initial value was measured.
[0066] 表 2の結果によれば、繰り返しアルカリ領域に pH調整した場合、 pHがより高い領域 ほど Fe2+イオン濃度が低下する傾向がみられる力 経時とともに pHが低下し、十分 に高い Fe2+イオン濃度が保たれる傾向は上記 (1)の場合と同様であることが分かる。 [0066] According to the results in Table 2, when pH is repeatedly adjusted to the alkaline region, the force that tends to decrease the Fe 2+ ion concentration in the region where the pH is higher. The pH decreases with time, and the Fe is sufficiently high. it can be seen tendency 2+ ion concentration is maintained is the same as in the above (1).
[0067] [3]アルカリ土壌用植物用鉄供給剤の製造及びその評価 (その 1) [0067] [3] Manufacture and evaluation of plant iron supply agent for alkaline soil (Part 1)
実験例 7 Experimental Example 7
(1)アルカリ土壌用植物用鉄供給剤 (A) 10%のァスコルビン酸(純度 99. 8%以上)と、 7. 5%の上記 [1]で製造した FeO 粉末と、 82. 5%の泥炭加工土壌改良剤(日本肥糧社製、商品名「くみあいハイフミ ン特号 A」)とを混合し、押出成形により造粒し、粒径 3〜6mmの略球体のアルカリ土 壌用植物用鉄供給剤 (A)を製造した。 (1) Plant iron supply agent for alkaline soil (A) 10% ascorbic acid (purity 99.8% or more), 7.5% FeO powder produced in [1] above, and 82.5% peat processing soil conditioner (trade name, manufactured by Nippon Fertilizer Co., Ltd.) “Kumiai Hyphen” (special name A)) was mixed and granulated by extrusion to produce a roughly spherical spherical iron supply agent (A) for alkaline soil plants.
[0068] (2)アルカリ土壌用植物用鉄供給剤の評価 [0068] (2) Evaluation of plant iron supply agent for alkaline soil
(A)イネの生育 (A) Rice growth
5個の栽培用ポットの各々に、下記の育苗用培土を投入し、シャーレを用いて発芽 させたイネ(品種;日本晴れ)の苗を発芽力も 3日後に植え付け、人工気象器を用い て生育させ、上記の植物成長促進剤 (A)の成長促進の作用、効果を評価した。 育苗用培土 (a);約 70質量%の CaCOを含有する貝化石土壌 100質量部 (以下、 In each of the five pots for cultivation, the following seedling culture soil was introduced, and the seedlings of rice (variety: Japan sunny day) that had been germinated using a petri dish were planted after 3 days, and grown using an artificial meteorological device. The growth promoting action and effect of the plant growth promoter (A) was evaluated. Raising soil for seedlings (a); 100 parts by mass of fossil shellfish soil containing about 70% by mass of CaCO
3 Three
部と略記する。 )に、肥料 (チッソ旭肥料社製、商品名「ロングトータル 70」) 1部を配 口し 7こ o Abbreviated as part. ) And fertilizer (made by Chisso Asahi Fertilizer Co., Ltd., trade name “Long Total 70”)
育苗用培土 (b);上記貝化石土壌 100部に、上記肥料 1部と上記植物用鉄供給剤 (A) 0. 1部とを配合した。 Seedling culture soil (b); 100 parts of the fossil shell soil was mixed with 1 part of the fertilizer and 0.1 part of the plant iron supply agent (A).
育苗用培土 (c);上記貝化石土壌 100部に、上記肥料 1部と上記植物用鉄供給剤 (A) 1部とを配合した。 Seedling soil (c); 100 parts of the fossil shell soil was mixed with 1 part of the fertilizer and 1 part of the plant iron supply agent (A).
人工気象器(日本医科器械製作所製、型式「LH— 100S」)は、日照を 14時間(照 度は 1500ルクス、温度は 25°C)、夜間を 10時間(温度は 20°C)に調整して運転した 。また、水は蒸発分の補充のみとした。即ち、アルカリ土壌における陸稲の生育を模 した運転条件とした。 Artificial meteorological device (manufactured by Nippon Medical Instrument Co., Ltd., model “LH-100S”) adjusts sunshine for 14 hours (light intensity is 1500 lux, temperature is 25 ° C) and night time is 10 hours (temperature is 20 ° C). And drove. In addition, water was only replenished by evaporation. In other words, operating conditions were set to simulate growth of upland rice in alkaline soil.
[0069] (B)評価結果 [0069] (B) Evaluation results
図 1は、上記 (A)のイネの生育における各々の苗の生育状況を発芽して 10日後に デジタル撮影して得られた画像による説明図である [図 1における(a)、 (b)及び (c) は、それぞれ上記育苗用培土 (a)、(b)及び (c)を用いた場合の結果を表している。 ] である。この説明図によれば、アルカリ土壌用植物用鉄供給剤 (A)を用いた (b)の場 合は、配合量が 0. 1部と少量であるにもかかわらず、肥料のみが配合された (a)と比 ベて苗の背が高ぐ順調に成長していることが分かる。また、アルカリ土壌用植物用 鉄供給剤 (A)の配合量が 1部である(c)では、(b)と比べてより苗の背が高ぐ特に順 調に成長して ヽることが分かる。 Fig. 1 is an explanatory diagram based on images obtained by digital photography 10 days after germination of the growth of each seedling in the growth of rice in (A) above ((a), (b) in Fig. 1) And (c) show the results of using the above seedling culture soil (a), (b) and (c), respectively. ] According to this explanatory diagram, in the case of (b) using the plant iron supply agent (A) for alkaline soil, only fertilizer is blended even though the blending amount is as small as 0.1 part. It can be seen that the seedlings are growing taller than (a). In addition, in (c) where the blending amount of the iron supply agent for plants for alkaline soil (A) is 1 part, the seedlings are particularly taller than (b). You can see that it grows well.
尚、各々の苗の色調にも明らかに差があり、(a)から (b)、特に (c)の順に苗の緑色 力 り強力つた。これによつて葉緑素量がより多 、ことが推察される。 There was also a clear difference in the color tone of each seedling, and the green strength of the seedlings was stronger in the order of (a) to (b), especially (c). This suggests that the amount of chlorophyll is higher.
[0070] [4]アルカリ土壌用植物用鉄供給剤の製造及びその評価 (その 2) [0070] [4] Manufacture and evaluation of plant iron supply for alkaline soil (Part 2)
実験例 8〜16 Experimental examples 8-16
(1)アルカリ土壌用植物用鉄供給剤 (B) (1) Plant iron supply agent for alkaline soil (B)
上記 [3]、(1)で製造したアルカリ土壌用植物用鉄供給剤 (A)を目開き 1. Ommの 篩を通過させ、粒径 1. Omm以下のアルカリ土壌用植物用鉄供給剤 (B)を得た。 The plant iron supply agent for alkaline soil (A) produced in [3] and (1) above is opened 1. Pass through an Omm sieve and have a particle size of 1. Omm for plant iron supply for alkaline soil ( B) was obtained.
(2)アルカリ土壌用植物用鉄供給剤 (C) (2) Plant iron supply agent for alkaline soil (C)
ァスコルビン酸(純度 99. 8%) 800gと水 2リットルとをステンレス鋼製ビーカーに投 入し、室温(20°C)で攪拌し、ァスコルビン酸を水に溶解させた。その後、上記 [1]で 製造した FeO粉末を 100g投入し、更に 30分間攪拌を継続した。次いで、この FeO 粉末分散液を濾紙を用いて濾過し、濾液を 90°Cに調温された乾燥機により 72時間 乾燥させた。その後、得られたペースト状物を室温まで冷却して塊状物とし、これを乳 鉢で十分に粉砕し、次いで、目開き 1. Ommの篩を通過させ、粒径 1. Omm以下の アルカリ土壌用植物用鉄供給剤 (C)を製造した。 Ascorbic acid (purity 99.8%) 800 g and 2 liters of water were put into a stainless steel beaker and stirred at room temperature (20 ° C) to dissolve ascorbic acid in water. Thereafter, 100 g of the FeO powder produced in [1] above was added, and stirring was continued for another 30 minutes. Next, this FeO powder dispersion was filtered using a filter paper, and the filtrate was dried for 72 hours by a drier adjusted to 90 ° C. Thereafter, the obtained paste-like material is cooled to room temperature to form a lump, which is sufficiently pulverized in a mortar, then passed through a sieve with an opening of 1. Omm, and an alkaline soil having a particle size of 1. Omm or less. An iron supply agent for plants (C) was produced.
[0071] (2)アルカリ土壌用植物用鉄供給剤の評価 [0071] (2) Evaluation of plant iron supply agent for alkaline soil
(A)イネの生育 (A) Rice growth
栽培用ポットの各々に、下記の育苗用培土を投入し、シャーレを用いて催芽させた イネ(品種;日本晴れ)の籾を 1ポット当たり 20粒づっ直播きした。籾は表面から約 0. 5cmの深さの培土中に埋め込んだ。その後、人工気象器を用いて生育させ、前記の 植物用鉄供給剤 (A)及び上記の植物用鉄供給剤 (B)及び (C)の成長促進の作用、 効果を評価した。 The following seedling culture soil was added to each of the cultivation pots, and 20 seeds of rice (variety: Nihonbare) sprouting using a petri dish were directly sown. The cocoons were embedded in the soil at a depth of about 0.5 cm from the surface. Then, it was grown using an artificial meteorograph, and the growth promoting action and effect of the above-mentioned plant iron supply agent (A) and the above-mentioned plant iron supply agents (B) and (C) were evaluated.
[0072] 苗は人工気象器(日本医科器械製作所製、型式「LH— 100S」)を用いて生育させ た。人工気象器は、 日照を 14時間(照度は 1500ルクス、温度は 25°C)、夜間を 10時 間(温度は 20°C)に調整して運転した。また、貝化石土壌 300mlに対して 50mlの蒸 留水を添加したものを圃場容水量とし、生育期間を通じて毎日ポットと内容物との全 重量力 OOgに維持されるように灌水した。更に、生育期間を通じて 13個のポットを 毎日ランダムに位置換えし、照明(日照)が均等に照射されるようにした。 [0072] The seedlings were grown using an artificial meteorological instrument (manufactured by Nippon Medical Instrumentation, model “LH-100S”). The artificial meteorograph was operated with sunshine adjusted to 14 hours (light intensity 1500 lux, temperature 25 ° C) and night time 10 hours (temperature 20 ° C). In addition, 50 ml of distilled water added to 300 ml of shell fossil soil was used as the field capacity, and irrigated so that the total weight of the pot and contents was maintained at OOg every day throughout the growing period. In addition, 13 pots throughout the growing period The position was changed randomly every day so that the illumination (sunshine) was evenly irradiated.
[0073] 実験例 8 ;上記ポット中の貝化石土壌に、肥料 (チッソ旭肥料社製、商品名「ロングト 一タル 70」) lgを配合し、育苗用培土とした。 Experimental Example 8: Fertilizer (manufactured by Chisso Asahi Fertilizer Co., Ltd., trade name “Long Total 70”) lg was blended in the shell fossil soil in the pot to prepare a seedling culture soil.
実験例 9 ;上記ポット中の貝化石土壌に、上記肥料 lgと、前記アルカリ土壌用植物 用鉄供給剤 (A) (表 1では種類の欄に A、性状の欄に粒体と表記する。以下、同様で ある。 ) 0. lgとを配合し、育苗用培土としたた。 Experimental Example 9: The fertilizer lg and the ferrous fertilizer for alkaline soil (A) (in Table 1, “A” in the column of type and “granule” in the column of property) in the shell fossil soil in the pot. The same shall apply hereinafter.) 0. lg was added to prepare a seedling culture soil.
実験例 10 ;上記ポット中の貝化石土壌に、上記肥料 lgと、上記アルカリ土壌用植 物用鉄供給剤 (B) (表 1では種類の欄に B、性状の欄に粉体と表記する。以下、同様 である。 ) 0. lgとを配合し、育苗用培土とした。 Experimental Example 10: The fertilizer lg and the ferrous fertilizer for alkaline soil (B) above the shell fossil soil in the pot (B in the type column and B in the property column and powder in the property column) The same shall apply hereinafter.) 0. lg was added to make a seedling culture soil.
実験例 11 ;上記ポット中の貝化石土壌に、上記肥料 lgと、前記アルカリ土壌用植 物用鉄供給剤 (A) l. Ogとを配合し、育苗用培土とした。 Experimental Example 11: The above fertilizer lg and the above-mentioned fertilizer for plant for alkaline soil (A) l.Og were blended with the fossil shell soil in the pot to prepare a seedling culture soil.
実験例 12 ;上記ポット中の貝化石土壌に、上記肥料 lgと、上記アルカリ土壌用植 物用鉄供給剤 (B) l. Ogとを配合し、育苗用培土とした。 Experimental Example 12: The above fertilizer lg and the above-mentioned fertilizer for plant for alkaline soil (B) l.Og were blended with the fossil shell soil in the pot to prepare a seedling culture soil.
実験例 13 ;上記ポット中の貝化石土壌に、上記肥料 lgと、前記アルカリ土壌用植 物用鉄供給剤 (A) 2. Ogとを配合し、育苗用培土とした。 Experimental Example 13: The above-mentioned fertilizer lg and the above-mentioned fertilizer for plant for alkaline soil (A) 2. Og were blended with the fossil shell fossil soil in the pot to prepare a seedling culture soil.
実験例 14 ;上記ポット中の貝化石土壌に、上記肥料 lgと、上記アルカリ土壌用植 物用鉄供給剤 (B) 2. Ogとを配合し、育苗用培土とした。 Experimental Example 14: The above-mentioned fertilizer lg and the above-mentioned fertilizer for plant for alkaline soil (B) 2. Og were blended with the fossil shell fossil soil in the pot to prepare a seedling culture soil.
実験例 15 ;上記ポット中の貝化石土壌に、上記肥料 lgと、上記アルカリ土壌用植 物用鉄供給剤 (C) (表 1では種類の欄に C、性状の欄に粉体と表記する。以下、同様 である。 ) 0. lgとを配合し、育苗用培土とした。 Experimental Example 15: Fertilizer lg and shell fertilizer for alkaline soil (C) (in Table 1, C in the type column and powder in the property column) The same shall apply hereinafter.) 0. lg was added to make a seedling culture soil.
実験例 16 ;上記ポット中の貝化石土壌に、上記肥料 lgと、上記アルカリ土壌用植 物用鉄供給剤 (C) l. Ogとを配合し、育苗用培土とした。 Experimental Example 16: The above-mentioned fertilizer lg and the above-mentioned fertilizer for plant for alkaline soil (C) l.Og were blended with the fossil shell fossil soil in the pot to prepare a seedling culture soil.
[0074] 上記のようにして生育させ、籾の直播きから 54日経過後に写真撮影をし、苗を収穫 した。また、収穫に先立ち各々のポットのそれぞれ 20本の苗の草丈を測定した。更に 、 SPAD値 (葉緑素量の指標である緑色濃度である。)を、葉緑素計 (ミノルタ株式会 社製、型式「SPAD— 502」)を用いて測定した。また、収穫時に根の土をふるい、そ の後、 7日間乾燥させ、次いで、再度根の土をふるい、ほぼ全量をふるい落とし、そ の後、写真撮影するとともに、地上部乾物重と根部乾物重 (根乾物重と籾重との合計 )とを測定した。 [0074] The seedlings were grown as described above, photographed 54 days after direct seeding of the pods, and harvested. Prior to harvesting, the plant height of 20 seedlings in each pot was measured. Further, the SPAD value (green density, which is an index of the amount of chlorophyll) was measured using a chlorophyll meter (model “SPAD-502” manufactured by Minolta Co., Ltd.). Sift the root soil at harvest, then dry for 7 days, then screen the root soil again to remove almost the entire amount, then take a picture and take the dry weight of the above ground and the dry weight of the root. (Total of dry root weight and weight ) Was measured.
結果を表 3及び図 2 11に記載する。 The results are shown in Table 3 and FIG.
尚、苗の草丈と SPAD値については、各々のポットのそれぞれ 20本の苗の平均値 と標準偏差とを記載した。 Regarding the plant height and SPAD value of seedlings, the average value and standard deviation of 20 seedlings in each pot are described.
[表 3] [Table 3]
[0076] (B)評価結果 [0076] (B) Evaluation result
実験例 9、 10によれば、実験例 10の SPAD値を除いて、植物用鉄供給剤が投与さ れていない実験例 8に比べて良好な結果となっている(図 2、 3、 7及び 8参照)。また 、この実験例 9、 10では、実験例 11〜14に比べて生育促進が十分ではなぐ更に多 くの植物用鉄供給剤の投与が望ましいことが分力る。 According to Experimental Examples 9 and 10, except for the SPAD value in Experimental Example 10, the results are better than in Experimental Example 8 in which no plant iron supplier was administered (Figures 2, 3, and 7). And 8). Further, in Experimental Examples 9 and 10, it is desirable to administer more plant iron supply agents that are not sufficiently promoted in growth compared with Experimental Examples 11 to 14.
[0077] 実験例 11、 12によれば、地上部乾物重及び根部乾物重は同等であるが(図 2、 3 及び 9参照)、実験例 12では SPAD値のばらつきが小さく(標準偏差値が低く)安定 している。即ち、粒体より粉体で投与したほうが土壌における鉄の溶解量が高くなり、 各々の苗の根と均等に接触し易ぐ苗間のばらつきが小さくなつたと推察される。一 方、実験例 13、 14によれば、地上部乾物重及び SPAD値は同程度であるが、実験 例 14では実験例 13より草丈がやや低い。これは、投与量が同じ 2gであっても、粉体 である実験例 14では鉄が溶解し過ぎ、やや過剰であることが理由であるの力もしれ ない。しかし、外見では鉄過剰症であるネクロシスを呈するほどではない(図 2及び 5 参照)。また、実験例 11、 12では、投与量が実験例 13、 14の半分量であるにもかか わらず、地上部乾物重はほぼ等しぐ根部乾物重は投与量の少ない実験例 11、 12 のほうが多く優れている(図 7参照)。これは、植物用鉄供給剤 (B)の投与量が 2gで は過剰であることを示唆して 、る。 [0077] According to Experimental Examples 11 and 12, the above-ground dry weight and root dry weight are the same (see Figs. 2, 3 and 9), but in Experimental Example 12, the dispersion of SPAD values is small (standard deviation value is Low) Stable. In other words, it is presumed that the amount of iron dissolved in the soil is higher when administered as powder than granules, and the variability between seedlings that easily come into contact with the roots of each seedling is reduced. On the other hand, according to Experimental Examples 13 and 14, the above-ground dry weight and SPAD values are similar, but in Experimental Example 14, the plant height is slightly lower than in Experimental Example 13. This may be due to the fact that even in the same dose of 2 g, iron 14 is too much dissolved and slightly excessive in Experimental Example 14, which is a powder. However, it does not appear to exhibit necrosis, an iron overload (see Figures 2 and 5). In Experimental Examples 11 and 12, the dry weight of the root part is almost equal to the dry weight of the root part, even though the dosage is half that of Experimental Examples 13 and 14. 12 is much better (see Figure 7). This suggests that the dose of plant iron supply (B) is excessive at 2 g.
[0078] 実験例 16では、草丈及び SPAD値ともに実験例のうちで最もよい結果となっている [0078] In Experimental Example 16, both the plant height and SPAD value are the best among the experimental examples.
(図 2及び 6参照)。この実験例 16に比べて植物用鉄供給剤 (C)の投与量が 1Z10 である実験例 15では、草丈、 SPAD値、地上部乾物重及び根部乾物重のすべてが 実験例 16に比べて低下した(図 2、 6、 7及び 11参照)。従って、実験例 15の投与量 では鉄の供給が十分ではないと推察される。一方、実験例 16では、鉄の過剰症はみ られないため、植物用鉄供給剤 (C)を更に多量に投与した場合、より生育が促進さ れる可能性がある。 (See Figures 2 and 6.) Compared with Experimental Example 16, in Experimental Example 15 where the dose of plant iron supplier (C) is 1Z10, plant height, SPAD value, aboveground dry weight and root dry weight all decreased. (See Figures 2, 6, 7 and 11). Therefore, it is assumed that the supply of iron is not sufficient at the dose of Experimental Example 15. On the other hand, in Experimental Example 16, there is no iron overload, and therefore growth may be further promoted when a higher amount of the plant iron supply agent (C) is administered.
尚、実験例 15では、 SPAD値は低いものの、草丈、地上部乾物重及び根部乾物 重は十分であり、優れている。これは、実験例 15では投与量が実験例 16の 1Z10で あるにもかかわらず、根の生育は実験例 16と同等であることを意味している。即ち、 鉄は根部の生育に優先的に利用され、その後、地上部の生育に利用されるのではな いかと推察される。 In Experimental Example 15, although the SPAD value is low, the plant height, the above-ground dry weight and the root dry weight are sufficient and excellent. This means that in Example 15, the growth of roots is equivalent to Example 16 although the dose is 1Z10 in Example 16. That is, iron should be used preferentially for root growth and then for ground growth. It is guessed how.
[0079] 尚、本発明では、上記の実施例の記載に限られず、本発明の範囲内で種々変更し た実施例とすることができる。例えば、ァスコルビン酸粉末と鉄成分粉末とを混合し、 この混合物に少量の水を添加し、その後、水を除去することにより得られる混合物を アルカリ土壌用植物用鉄供給剤として用いることもできる。この場合、ァスコルビン酸 粉末に対する水の量は特に限定されないが、通常、ァスコルビン酸粉末 100質量部 に対して水は 5〜20質量部、より好ましくは 5〜15質量部である。一方、鉄成分粉末 は、ァスコルビン酸粉末を 100質量部とした場合に、 10〜25質量部、特に 20〜25 質量部配合することができる。 [0079] It should be noted that the present invention is not limited to the description of the above-described embodiment, and various modifications can be made within the scope of the present invention. For example, a mixture obtained by mixing ascorbic acid powder and iron component powder, adding a small amount of water to the mixture, and then removing the water can be used as an iron supply agent for plants for alkaline soil. In this case, the amount of water relative to the ascorbic acid powder is not particularly limited, but is usually 5 to 20 parts by mass, more preferably 5 to 15 parts by mass with respect to 100 parts by mass of the ascorbic acid powder. On the other hand, the iron component powder can be blended in an amount of 10 to 25 parts by mass, particularly 20 to 25 parts by mass, based on 100 parts by mass of ascorbic acid powder.
上記のァスコルビン酸粉末及び鉄成分粉末につ 、ては、前記の記載をそのまま適 用することができる。また、上記のように少量の水を用いて得られた固形物又はぺー スト状物における水分量は、本他の植物用鉄供給剤と同程度とすることができる。更 に、水の除去方法も本他の植物用鉄供給剤のときと同様とすることができ、減圧加熱 乾燥が好ましい。また、水を除去する際に加熱する場合の温度、及び水を除去する 際に減圧にする場合の圧力も、本他の植物用鉄供給剤のときと同様とすることができ る。 For the above ascorbic acid powder and iron component powder, the above description can be applied as it is. In addition, the water content in the solid or paste-like material obtained by using a small amount of water as described above can be set to the same level as the other iron supply agents for plants. Further, the water removal method can be the same as that for the other iron supply agents for plants, and drying under reduced pressure is preferable. In addition, the temperature at the time of heating when removing water and the pressure at which the pressure is reduced when removing water can be the same as those of other iron supply agents for plants.
産業上の利用可能性 Industrial applicability
[0080] 本発明のアルカリ土壌用植物用鉄供給剤は、農林分野において広く利用される。 [0080] The plant iron supply agent for alkaline soil of the present invention is widely used in the field of agriculture and forestry.
即ち、例えば、農産物の生産、水耕栽培、園芸植物の生産、公園及びゴルフ場の植 生の保持、森林保持等に幅広く利用される。また、特に各種農産物の生産分野にお ける植物成長促進剤として有用である。更に、世界各地の不毛の土地での植物の成 長による食料問題の解決、及び二酸化炭素の吸収促進による地球環境の改善等に 禾 IJ用することちでさる。 That is, for example, it is widely used for production of agricultural products, hydroponics, production of horticultural plants, maintenance of vegetation in parks and golf courses, maintenance of forests, and the like. In particular, it is useful as a plant growth promoter in the field of production of various agricultural products. Furthermore, it can be used to solve food problems caused by plant growth in barren lands around the world and to improve the global environment by promoting absorption of carbon dioxide.
Claims
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| JP2007528361A JP4096208B2 (en) | 2005-07-29 | 2006-05-29 | Iron supply agent for plant for alkaline soil and method for producing the same |
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| JP2005-220024 | 2005-07-29 | ||
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| PCT/JP2006/310702 Ceased WO2007013219A1 (en) | 2005-07-29 | 2006-05-29 | Iron supplying agent for plant for use in alkaline soil, and process for production of the same |
| PCT/JP2006/310701 Ceased WO2007013218A1 (en) | 2005-07-29 | 2006-05-29 | Iron-supplying agent, iron supplying agent for plant comprising the same, and process for production of the same |
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| JP (2) | JP4096208B2 (en) |
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| JP2010228951A (en) * | 2009-03-26 | 2010-10-14 | Aichi Steel Works Ltd | Iron supplier for plant and method for manufacturing the same |
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Also Published As
| Publication number | Publication date |
|---|---|
| JP4096207B2 (en) | 2008-06-04 |
| WO2007013218A1 (en) | 2007-02-01 |
| JPWO2007013218A1 (en) | 2009-02-05 |
| TW200738583A (en) | 2007-10-16 |
| JPWO2007013219A1 (en) | 2009-02-05 |
| JP4096208B2 (en) | 2008-06-04 |
| TW200704623A (en) | 2007-02-01 |
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