WO1992015539A1 - Verfahren zur herstellung homogener, feiner, pulverförmiger, gegebenenfalls wirkstoffe enthaltender feststoffdispersionen - Google Patents
Verfahren zur herstellung homogener, feiner, pulverförmiger, gegebenenfalls wirkstoffe enthaltender feststoffdispersionen Download PDFInfo
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- WO1992015539A1 WO1992015539A1 PCT/EP1992/000436 EP9200436W WO9215539A1 WO 1992015539 A1 WO1992015539 A1 WO 1992015539A1 EP 9200436 W EP9200436 W EP 9200436W WO 9215539 A1 WO9215539 A1 WO 9215539A1
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- clay
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
- B09B—DISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
- B09B1/00—Dumping solid waste
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/50—Mixing liquids with solids
- B01F23/51—Methods thereof
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/02—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
- B01J20/0203—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising compounds of metals not provided for in B01J20/04
- B01J20/0225—Compounds of Fe, Ru, Os, Co, Rh, Ir, Ni, Pd, Pt
- B01J20/0229—Compounds of Fe
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/02—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
- B01J20/0203—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising compounds of metals not provided for in B01J20/04
- B01J20/0248—Compounds of B, Al, Ga, In, Tl
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/02—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
- B01J20/0203—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising compounds of metals not provided for in B01J20/04
- B01J20/0274—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising compounds of metals not provided for in B01J20/04 characterised by the type of anion
- B01J20/0277—Carbonates of compounds other than those provided for in B01J20/043
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/02—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
- B01J20/0203—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising compounds of metals not provided for in B01J20/04
- B01J20/0274—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising compounds of metals not provided for in B01J20/04 characterised by the type of anion
- B01J20/0285—Sulfides of compounds other than those provided for in B01J20/045
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/02—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
- B01J20/0203—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising compounds of metals not provided for in B01J20/04
- B01J20/0274—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising compounds of metals not provided for in B01J20/04 characterised by the type of anion
- B01J20/0292—Phosphates of compounds other than those provided for in B01J20/048
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/02—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
- B01J20/04—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising compounds of alkali metals, alkaline earth metals or magnesium
- B01J20/041—Oxides or hydroxides
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/02—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
- B01J20/04—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising compounds of alkali metals, alkaline earth metals or magnesium
- B01J20/045—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising compounds of alkali metals, alkaline earth metals or magnesium containing sulfur, e.g. sulfates, thiosulfates, gypsum
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/02—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
- B01J20/10—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising silica or silicate
- B01J20/12—Naturally occurring clays or bleaching earth
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/28—Treatment of water, waste water, or sewage by sorption
- C02F1/288—Treatment of water, waste water, or sewage by sorption using composite sorbents, e.g. coated, impregnated, multi-layered
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
- C02F1/5236—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using inorganic agents
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- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B28/00—Compositions of mortars, concrete or artificial stone, containing inorganic binders or the reaction product of an inorganic and an organic binder, e.g. polycarboxylate cements
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- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B28/00—Compositions of mortars, concrete or artificial stone, containing inorganic binders or the reaction product of an inorganic and an organic binder, e.g. polycarboxylate cements
- C04B28/001—Compositions of mortars, concrete or artificial stone, containing inorganic binders or the reaction product of an inorganic and an organic binder, e.g. polycarboxylate cements containing unburned clay
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- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
- C09K17/00—Soil-conditioning materials or soil-stabilising materials
- C09K17/02—Soil-conditioning materials or soil-stabilising materials containing inorganic compounds only
- C09K17/04—Soil-conditioning materials or soil-stabilising materials containing inorganic compounds only applied in a physical form other than a solution or a grout, e.g. as granules or gases
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2220/00—Aspects relating to sorbent materials
- B01J2220/40—Aspects relating to the composition of sorbent or filter aid materials
- B01J2220/42—Materials comprising a mixture of inorganic materials
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2220/00—Aspects relating to sorbent materials
- B01J2220/40—Aspects relating to the composition of sorbent or filter aid materials
- B01J2220/48—Sorbents characterised by the starting material used for their preparation
- B01J2220/4875—Sorbents characterised by the starting material used for their preparation the starting material being a waste, residue or of undefined composition
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/91—Use of waste materials as fillers for mortars or concrete
Definitions
- Solid dispersions play an important role in the agricultural field and in technology. Examples are clay flours, which play an important role as soil improvers and as adsorbents in industrial processes. If finely dispersed solid dispersions from finely dispersed, water-containing precursors, e.g. to be produced from natural clay, this requires thermally complex drying processes with a subsequent mechanical homogenization. If finely dispersed solid dispersions are to be produced from coarse-grained solids or solid components, mechanically complex grinding or grinding processes are required to obtain solid dispersions which are largely finely dispersed and homogeneous; These mechanical processes are in any case limited by the fact that the grain size that can be achieved in this case is determined solely by the maximum technically achievable shear forces.
- the invention is therefore based on the object of providing a process by which extraordinarily homogeneous and finely dispersed solid dispersions can be prepared without any particular technical outlay.
- a water-containing, finely dispersed solid suspension is mechanically homogenized with an educt of a water-consuming chemical reaction, for example with an alkaline earth metal oxide or an aluminum alcoholate or a silicic acid ester or a mixture of these compounds, and the homogenate is then left with the stoichiometric consumption required amount of water react completely.
- the water-consuming reaction chosen is a reaction in which a finely dispersed solid is formed from the educt; Accordingly, alkaline earth metal hydroxides or aluminum hydroxides - > or silicic acid are formed from the starting materials mentioned.
- Aqueous, finely dispersed solid suspensions which can be used for the purposes of the invention are suspensions of finely dispersed solids in water.
- Finely dispersed substances in the sense of the invention are substances with particle sizes in the range of
- finely disperse solid suspensions preferably > 0 to ⁇ 250 micrometers, preferably in the range from 1 to 50 micrometers, which have a good adsorption capacity due to their structural characteristics.
- Examples are layered silicates, finely dispersed silica, aluminum oxides and aluminum hydroxides, precipitated chalk and iron oxides. Their pasty mixtures with water are referred to here as finely disperse solid suspensions.
- the water content in the finely dispersed solid suspension may fluctuate within wide limits, provided that there is sufficient water on the one hand for the subsequent chemical reaction with an alkaline earth metal oxide or aluminum alcoholate and on the other hand that there is no longer any water, such as for the production of a powdery solid dispersion.
- the water content of the finely dispersed solid suspension is preferably adjusted such that a pasty, kneadable mass is present.
- the water-containing, finely dispersed solid suspensions can be of natural or industrial origin.
- a pasty and kneadable, water-containing, finely dispersed solid suspension of natural origin is clay, as it is obtained in pits for the production of clay, and which can still be used according to the invention.
- Bleaching earth and clay flours are of industrial origin; if they are pasted with water, water-containing, finely dispersed solid suspensions are obtained which are likewise useful in the sense of the invention.
- clay-like and clay-containing materials can also be used to produce water-containing, finely dispersed solid suspensions. If one speaks of clay-like and clay-containing materials, this refers solely to their adsorption capacity due to physical and structural characteristics and not to the chemical composition.
- Examples are clay-like or clay-like fly dusts, filter dusts, ashes and production residues, e.g. production residues from the food industry in the form of used bleaching earth, or e.g. red mud, a pasty mass vorweige ⁇ d made of iron oxides and iron hydroxides, which is obtained in connection with the production of aluminum.
- solid and liquid active ingredients can be mechanically applied to a solid carrier by grinding.
- a solid carrier can also be impregnated with an active ingredient solution and the suspension then dried. Suitable active ingredients can be evaporated onto a solid carrier.
- the invention therefore also has the object of producing powdery solid dispersions homogeneously loaded with active ingredients in a technically simple and thus economical manner and largely avoiding limitations and disadvantages.
- a water-containing, finely disperse solid suspension is mechanically homogenized with active substances or mixtures of active substances, and the homogenate is then homogenized with an alkaline earth oxide or an aluminum alcoholate.
- the latent adsorption capacity of the solids in finely dispersed form in a water-containing solid suspension which are completely coated with water in this environment and are therefore practically incapable of adsorption, is made usable when the water-containing solid suspension is present
- Active substances which can be adsorbed, distributed homogeneously and which may be present as a solution or in a finely dispersed suspension, by a water-consuming reaction, for example by the hydration reaction of an alkaline earth metal oxide or by the hydrolysis of an aluminum alcoholate, chemically remove the water, so that the active substances be adsorptively bound to the surface of the now largely water-free solid.
- the finely disrupted reaction resulting from the starting material of a water-consuming reaction persistent, solid reaction product for example finely dispersed alkaline earth metal or aluminum hydroxide made of alkaline earth oxide or aluminum alcoholate, also has an adsorptive effect.
- the advantage of the invention is based on the fact that, unlike in mechanical dispersing, even small amounts of active ingredient can be homogeneously distributed on a solid carrier, and that, unlike in the case of a homogeneous fine distribution of active ingredients in the course of dispersing chemical reactions, the indispensable prerequisite there. namely the predistributability of the active ingredients to be distributed in the starting material of the dispersing chemical reaction, for example in an alkaline earth oxide, aluminum alcoholate or silicic acid ester is absolutely not necessary.
- the active ingredient in order to produce a powdery solid dispersion homogeneously loaded with active ingredients, the active ingredient is mechanically homogenized with a water-containing, finely dispersed solid suspension and the homogenized product is only then homogenized with an alkaline earth metal oxide or aluminum alcoholate.
- the proportion of alkaline earth oxide or aluminum alcoholate required to produce a powdery solid dispersion homogeneously loaded with active ingredients can be reduced considerably, in favorable cases to about a tenth of the amount required for a dispersing chemical reaction.
- active substances are substances that, in contrast to the substances in the solid suspension that are considered to be mere carriers, are particularly effective in chemical and physical terms in their finely divided state. In this context, too, it is not the physical and chemical properties of the substances involved that matter, but only the role that is assigned to them for the respective application. This. will be explained using two examples. Natural clay is homogenized by kneading with a concentrated aqueous solution of sodium sulfide; The resulting plastic mass in the subsequent water-consuming chemical reaction with about 15% hydrophobic calcium oxide, based on the amount of clay used, results in a powdery solid dispersion homogeneously loaded with sulfide ions.
- the finely divided active ingredient sulfide ions is known to be a highly reactive precipitation reagent with which numerous toxic heavy metals can be converted into water-insoluble heavy metal sulfides by precipitation and can thus be chemically fixed and immobilized.
- soils, fly ash, slags contaminated with heavy metals are mixed with the solid dispersion mentioned and then compacted to give a solid body.
- Coarse-particle contaminated materials for example chimney linings, foundation parts, equipment and the like, are embedded in the solid dispersion as such or in a mixture with other materials which are advantageous from a soil mechanical point of view, with compaction.
- the soil mechanics aspect plays a particularly important role in the treatment of heavy metal contaminated sewage sludge with its soil mechanically unstable gel structures in order to be able to deposit them safely after homogenization with the solid dispersion mentioned in the form of soil mechanically stable and stable soil bodies.
- Mixing in suitable waste materials contaminated with heavy metals, such as slags and ashes, is particularly advantageous from an economic point of view.
- a part of the clay is first kneaded with an aqueous alkali sulfide solution and a second part with a fine-grained aqueous suspension of iron sulfate. If the two subsets are then homogenized, iron sulfide which is very finely divided in situ and embedded in the clay structure is formed.
- the still pasty mass is now chemically converted with about 20%, based on the total amount of clay, of normal, ie not hydrophobicized, calcium oxide. The stoichiometric proportions are chosen so that there is a slight excess of iron ions, for example 10%.
- the active ingredient now consists of iron sulfide, which is considered to be water-insoluble.
- substances are used with the sulfides mentioned which, owing to their chemical reactivity, in particular as a precipitation reagent, can be readily addressed as active ingredients.
- Active substances within the meaning of the invention can also be substances that are considered chemically inert.
- hard bitumen is melted, kneaded with clay and, as soon as it is homogeneous, this mass is mixed with calcium oxide, preferably with hydrophobic calcium oxide, and then kneaded again, the water-consuming hydration reaction of the calcium oxide begins after some time. and the originally pasty mass disintegrates into a powdery, homogeneously loaded with hard bitumen
- Solid dispersion The calcium hydroxide contained in this solid dispersion is known to be in no way inert from a chemical point of view, but has strongly basic properties and can therefore be easily, e.g. react with carbon dioxide, while the hard bitumen also contained in this solid dispersion is completely inert from a chemical point of view.
- the mixture of clay particles and calcium hydroxide present in the solid dispersion is the carrier and. the hard bitumen the active ingredient if the task. it consists, for example, of highly toxic organic pollutants, such as polychlorinated biphenyls (PCB) or dioxins and dibenzofurans (PCDD / PCDF), for example as ingredients in filter dusts from waste incineration plants or as contaminants in soils, by irreversible immobilization.
- PCB polychlorinated biphenyls
- PCDD / PCDF dioxins and dibenzofurans
- contaminated flue dusts or soils are mixed with a powdered solid dispersion loaded with hard bitumen, which was produced using clay and calcium oxide, and a soil body is produced from the mixture with compaction.
- the finely dispersed hard bitumen in the solid matrix incorporated the organic pollutants, because of their good solubility in the solid solvent hard bitumen. Leaching tests under long-term conditions and using trace analysis methods prove that. organic pollutants treated in accordance with the invention remain permanently and completely immobilized. Other high-boiling organic inert substances, such as hard paraffin, petroleum jelly or mineral oil, can take the place of hard bitumen.
- plant nutrients of the most varied types can be processed into extraordinarily homogeneous long-term fertilizers, provided they are stable in the resulting alkaline medium.
- the number of active ingredients that can be used in the environmental protection field is unmanageably large because the number of pollutants with problems is so large.
- high-boiling organic phases are particularly important as active ingredients for the adsorption and absorption of inorganic and organic pollutants, because this form of immobilization and physical fixation is particularly simple and comprehensive;
- One example among many is the absorptive removal of pollutants from waste gases from waste incineration plants using long-chain amines as active ingredients.
- hydrophobic calcium oxide is preferably used. It is part of the essence of the invention that the water contained in the finely dispersed solid suspension is consumed uniformly in the chemical reaction with alkaline earth oxide or aluminum alcoholate, because only under this condition can a homogeneously loaded powdery solid dispersion be formed. For this reason, the water-consuming reaction may only start when the alkaline earth metal oxide or aluminum alcoholate is uniformly distributed in the homogenate of active ingredient and solid suspension.
- 100 parts by weight of a natural plastic clay are homogenized in a kneader with 18 parts by weight of a calcium oxide hydrophobicized with 1% fatty acid.
- the hydration reaction which begins after about 5 minutes is allowed to run outside the kneader; this results in an extraordinarily homogeneous solid dispersion of calcium hydroxide in clay, which is so homogeneous that the components themselves can no longer be seen under the microscope.
- plastic clay is kneaded first with 2% potassium sulfate as a reaction retardant and then with non-hydrophobized calcium oxide. The hydration reaction only begins after about 20 minutes.
- red mud is used or a paste consisting of 70 parts by weight of dry, used bleaching earth and 30 parts by weight of water.
- 70 parts by weight of clay, 7.6 parts by weight of iron sulfate FeSO. x 7H 0.3 parts by weight of sodium sulfide Na_S (60%) and 4 parts by weight of water are homogenized in a kneader.
- the homogenate is homogenized with 15.4 parts by weight of calcium oxide.
- 100 parts by weight of a pulverulent solid dispersion which is homogeneously loaded with 2% iron sulfide FeS and can be used to precipitate heavy metals in contaminated materials.
- the proportion of iron sulfate is such that there is a 20% excess in relation to the stoichiometrically required amount; In this way it is prevented that soluble alkali sulfide, for example in the treatment of contaminated soils or contaminated production residues, can get into the groundwater in the course of the treatment according to the invention.
- the clay in this example can be replaced in whole or in part by pastes of dry, used bleaching earth with water, for example 77 parts by weight of used bleaching earth from the food industry with 23 parts by weight of water or with so-called red mud, or by pasting a finely disperse Filter dust with so much water that a clay-like matrix is created.
- reaction retarders is not necessary in this example because, in analogy to the alkali sulfates, the iron sulfate already delays the chemical reaction of the calcium oxide in such a way that complete homogenization is possible before the water-consuming reaction of the calcium oxide begins.
- Example 2 35 parts by weight of clay are homogenized with a suspension of 7.6 parts by weight of iron sulfate and 2 parts by weight of water in a compulsory mixer; 35 parts by weight of clay are mixed with an aqueous solution of
- both portions are homogenized in a compulsory mixer and then homogenized with 15.4 parts by weight of hydrophobic calcium oxide.
- the result is a powdery solid dispersion which is loaded extremely homogeneously with 2% iron sulfide FeS and which, like that from Example 1, can be used.
- the separately prepared homogenates of clay and iron sulfate or of clay and sodium sulfide are homogenized with 7.7 parts by weight of calcium oxide and hydrophobic calcium oxide, respectively.
- Mixing the two pulverulent solid dispersions loaded with iron hydroxide or sodium sulfide gives a preparation which, in the presence of an excess of hydrophobic calcium hydroxide, can be used particularly effectively and at the same time in an environmentally friendly manner for the treatment of heavy metal-containing, binding materials because, on the one hand, the The heavy metals are precipitated immediately with the aid of the alkali sulfide, but on the other hand no trace of this sulfide can get into the environment, because it is trapped by the iron hydroxide present, without the precipitating effect on heavy metals which have not yet been eliminated becomes.
- the melted bitumen is mixed, for example, with the required amount of an active ingredient which contains a functional group capable of reacting with the pollutant, so that the adsorption equilibrium is shifted towards complete absorption becomes.
- a commercially available aluminum mixed alcoholate e.g.
- the clay can be replaced particularly advantageously by red mud, because this finely dispersed system adsorbs the dioxins and furans mentioned particularly effectively in the dry state.
- 150 parts by weight of clay with a water content of 23% are plasticized with 10 parts by weight of water in a kneader and 1 part by weight of a water-soluble salt of copper or manganese, or zinc, or molybdenum or boron or iron, for example in the form of the corresponding copper, iron, manganese and zinc sulfates, or as ammonium molybdate or potassium metaborate.
- the homogenates are then mixed in with an alkaline earth oxide mixture of 90% calcium oxide and 10% magnesium oxide, which has been made hydrophobic with 0.2% fatty acid homogenized in a kneader.
- the individually obtained homogeneous, powdery solid dispersions loaded with the trace elements mentioned are mixed in a downpipe mixer in a proportion required according to the task.
- An additive for substrate production from peat or compost is obtained.
- the hydrophobic properties of the additive cause rapid mixing even with very moist peat or compost. If one speaks here of the mixing ratio according to the task at hand, this means the different needs of the plants in their different growth phases.
- the clay in the corresponding preparation is additionally homogenized with 1 part by weight of tartaric acid or for a further increase in bioavailability with 1 part by weight of citro nenoic acid.
- a double excess of the stoichiometrically required amounts of dipotassium hydrogen phosphate, iron sulfide and calcium carbonate are converted analogously to the procedure in Example 1 separately into homogeneous solid dispersions using calcium oxide which has been hydrophobized with 1% fatty acid.
- the mixture of the individual solid dispersions is particularly suitable for irreversibly immobilizing heavy metal ions in sewage sludge, compost, river and harbor silt by precipitating the individual heavy metals as carbonates, sulfides and phosphates.
- Arsenic and antimony can also be chemically fixed in this way.
- the solid dispersions mentioned are mixed into the waste materials to be treated simultaneously with additional, slightly hydrophobicized calcium oxide, e.g.
- 100 parts by weight of clay or a paste of finely dispersed aluminum hydroxide or zeolite or bentonite with water or used, moist bleaching earth, or 100 parts by weight of a mixture of the solid suspensions mentioned are mixed with 50 parts by weight of a long-chain amine, for example stearylamine, and 10 parts by weight of an aminosilane, for example a trialkoxy aminosilan ⁇ , homogenized in a kneader and then homogenized with 500 parts by weight of hydrophobic calcium oxide.
- a long-chain amine for example stearylamine
- an aminosilane for example a trialkoxy aminosilan ⁇
- the resulting dry, powdery and homogeneous solid dispersion which contains an excess of calcium oxide, can be used as such or after the hydration reaction has elapsed, with not quite the stoichiometrically required amount of water in relation to the calcium oxide excess, in the form of the subsequent product, ie with calcium hydroxide as the predominant component in terms of quantity, use for the greatest possible absorption or absorption of pollutants in the exhaust gases of waste incineration plants, in particular of halogenated dibenzodioxins and dibenzofurans.
- Aluminum hydroxide or zeolite or bentonite with water, or used, moist bleaching earth, or 100 parts by weight of a mixture of the solid suspensions mentioned are homogenized with 50 parts by weight of an alkali or alkaline earth metal sulfide in a kneader and then with 150 parts by weight of hydrophobic Calcium oxide homogenized.
- the resulting dry, powdery and homogeneous solid dispersion, which contains an excess of calcium oxide can, because of its hydrophobic character, be easily incorporated into the surface of heaps which consist of production residues containing heavy metals. In this way, a comprehensive depot with precipitation reagents is created, which, due to slow desorption processes
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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Analytical Chemistry (AREA)
- Ceramic Engineering (AREA)
- Life Sciences & Earth Sciences (AREA)
- Dispersion Chemistry (AREA)
- Environmental & Geological Engineering (AREA)
- Materials Engineering (AREA)
- Water Supply & Treatment (AREA)
- Structural Engineering (AREA)
- Hydrology & Water Resources (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Soil Sciences (AREA)
- Geochemistry & Mineralogy (AREA)
- Processing Of Solid Wastes (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
- Fertilizers (AREA)
- Soil Conditioners And Soil-Stabilizing Materials (AREA)
- Treating Waste Gases (AREA)
- Treatment Of Sludge (AREA)
- Colloid Chemistry (AREA)
- Inorganic Compounds Of Heavy Metals (AREA)
Abstract
Description
Claims
Priority Applications (5)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP92504663A JPH05507440A (ja) | 1991-03-01 | 1992-02-28 | 均一に微細に分散された粉体状の固形分散生成物の製造方法および必要な場合は活性物質を均一に混入させた粉体状の固形分散生成物並びにこれらによって得られた製品の使用方法 |
| BR9204785A BR9204785A (pt) | 1991-03-01 | 1992-02-28 | Processo para a preparacao de dispersoes de solidos homogeneas,finas,em forma de po,eventualmente contendo substancias ativas |
| KR1019920702715A KR100220560B1 (ko) | 1991-03-01 | 1992-02-28 | 선택적으로 활성물질을 함유하는 균질의 미세한 분상 고체분산물을 생산하는 방법 |
| AU12055/92A AU648391B2 (en) | 1991-03-01 | 1992-02-28 | Homogeneous, finely dispersed, pulverulent solid dispersions |
| NO924190A NO301222B1 (no) | 1991-03-01 | 1992-10-30 | Fremgangsmåte for fremstilling av homogene, fine, pulverformige faststoffdispersjoner, samt anvendelse av dispersjonene |
Applications Claiming Priority (4)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DEP4106516.6 | 1991-03-01 | ||
| DE4106515A DE4106515C2 (de) | 1991-03-01 | 1991-03-01 | Verfahren zur Herstellung einer mit Wirkstoffen homogen beladenen, pulverförmigen, feindispersen Dispersion sowie die Verwendung danach erhaltener Produkte |
| DEP4106515.8 | 1991-03-01 | ||
| DE19914106516 DE4106516C2 (de) | 1991-03-01 | 1991-03-01 | Verfahren zur Herstellung einer pulverförmigen, homogenen, feindispersen Dispersion sowie die Verwendung danach erhaltener Produkte |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| WO1992015539A1 true WO1992015539A1 (de) | 1992-09-17 |
Family
ID=25901501
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/EP1992/000436 Ceased WO1992015539A1 (de) | 1991-03-01 | 1992-02-28 | Verfahren zur herstellung homogener, feiner, pulverförmiger, gegebenenfalls wirkstoffe enthaltender feststoffdispersionen |
Country Status (7)
| Country | Link |
|---|---|
| EP (1) | EP0527984A1 (de) |
| JP (1) | JPH05507440A (de) |
| KR (1) | KR100220560B1 (de) |
| AU (1) | AU648391B2 (de) |
| CA (1) | CA2081307A1 (de) |
| NO (1) | NO301222B1 (de) |
| WO (1) | WO1992015539A1 (de) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US10843273B2 (en) | 2015-12-08 | 2020-11-24 | Quantum Chemical Technologies (Singapore) Pte. Ltd. | Methods of purifying nanostructures |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE19903986A1 (de) * | 1999-02-02 | 2000-08-10 | Friedrich Boelsing | Verfahren zur reduktiven Dehalogenierung von Halogenkohlenwasserstoffen |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE204665C (de) * | ||||
| DE2533791A1 (de) * | 1975-07-29 | 1977-02-03 | Boelsing Friedrich | Verfahren zur herstellung von organische oder anorganische stoffe in feiner verteilung enthaltenen hydroxiden |
| FR2319407A1 (fr) * | 1975-07-29 | 1977-02-25 | Boelsing Friedrich | Procede de dispersion homogene de matiere et de melanges de matieres au cours de la production de preparation en poudre par reaction chimique |
| WO1988002268A1 (fr) * | 1986-09-24 | 1988-04-07 | Boelsing Friedrich | Procede pour deshalogener des hydrocarbures |
| WO1988002269A1 (fr) * | 1986-09-24 | 1988-04-07 | Boelsing Friedrich | Procede pour immobiliser des substances nocives dans la terre ou dans des matieres analogues a la terre |
-
1992
- 1992-02-28 EP EP92905319A patent/EP0527984A1/de not_active Withdrawn
- 1992-02-28 KR KR1019920702715A patent/KR100220560B1/ko not_active Expired - Fee Related
- 1992-02-28 CA CA002081307A patent/CA2081307A1/en not_active Abandoned
- 1992-02-28 WO PCT/EP1992/000436 patent/WO1992015539A1/de not_active Ceased
- 1992-02-28 AU AU12055/92A patent/AU648391B2/en not_active Ceased
- 1992-02-28 JP JP92504663A patent/JPH05507440A/ja active Pending
- 1992-10-30 NO NO924190A patent/NO301222B1/no unknown
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE204665C (de) * | ||||
| DE2533791A1 (de) * | 1975-07-29 | 1977-02-03 | Boelsing Friedrich | Verfahren zur herstellung von organische oder anorganische stoffe in feiner verteilung enthaltenen hydroxiden |
| FR2319407A1 (fr) * | 1975-07-29 | 1977-02-25 | Boelsing Friedrich | Procede de dispersion homogene de matiere et de melanges de matieres au cours de la production de preparation en poudre par reaction chimique |
| WO1988002268A1 (fr) * | 1986-09-24 | 1988-04-07 | Boelsing Friedrich | Procede pour deshalogener des hydrocarbures |
| WO1988002269A1 (fr) * | 1986-09-24 | 1988-04-07 | Boelsing Friedrich | Procede pour immobiliser des substances nocives dans la terre ou dans des matieres analogues a la terre |
Non-Patent Citations (1)
| Title |
|---|
| WORLD PATENTS INDEX LATEST Week 8850, Derwent Publications Ltd., London, GB; AN 88-354759 & DE,A,3 717 848 (RH WESTFAL KALKWERK & RH WESTF ELECTRIZIT AG) 8. Dezember 1988 * |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US10843273B2 (en) | 2015-12-08 | 2020-11-24 | Quantum Chemical Technologies (Singapore) Pte. Ltd. | Methods of purifying nanostructures |
Also Published As
| Publication number | Publication date |
|---|---|
| AU648391B2 (en) | 1994-04-21 |
| JPH05507440A (ja) | 1993-10-28 |
| AU1205592A (en) | 1992-10-06 |
| CA2081307A1 (en) | 1992-09-02 |
| NO924190D0 (no) | 1992-10-30 |
| KR100220560B1 (ko) | 1999-09-15 |
| NO301222B1 (no) | 1997-09-29 |
| EP0527984A1 (de) | 1993-02-24 |
| NO924190L (no) | 1992-10-30 |
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