EP0560802A1 - Procede de fabrication de granulats de zeolite. - Google Patents

Procede de fabrication de granulats de zeolite.

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Publication number
EP0560802A1
EP0560802A1 EP91920221A EP91920221A EP0560802A1 EP 0560802 A1 EP0560802 A1 EP 0560802A1 EP 91920221 A EP91920221 A EP 91920221A EP 91920221 A EP91920221 A EP 91920221A EP 0560802 A1 EP0560802 A1 EP 0560802A1
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EP
European Patent Office
Prior art keywords
weight
zeolite
liquid
granules
water
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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Application number
EP91920221A
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German (de)
English (en)
Other versions
EP0560802B2 (fr
EP0560802B1 (fr
Inventor
Werner Pichler
Jochen Jacobs
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Henkel AG and Co KGaA
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Henkel AG and Co KGaA
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Classifications

    • C—CHEMISTRY; METALLURGY
    • C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11D—DETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
    • C11D17/00—Detergent materials or soaps characterised by their shape or physical properties
    • C11D17/06—Powder; Flakes; Free-flowing mixtures; Sheets
    • C11D17/065—High-density particulate detergent compositions
    • C—CHEMISTRY; METALLURGY
    • C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11D—DETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
    • C11D3/00—Other compounding ingredients of detergent compositions covered in group C11D1/00
    • C11D3/02—Inorganic compounds ; Elemental compounds
    • C11D3/12—Water-insoluble compounds
    • C—CHEMISTRY; METALLURGY
    • C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11D—DETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
    • C11D3/00—Other compounding ingredients of detergent compositions covered in group C11D1/00
    • C11D3/02—Inorganic compounds ; Elemental compounds
    • C11D3/12—Water-insoluble compounds
    • C11D3/124—Silicon containing, e.g. silica, silex, quartz or glass beads
    • C11D3/1246—Silicates, e.g. diatomaceous earth
    • C11D3/128—Aluminium silicates, e.g. zeolites
    • C—CHEMISTRY; METALLURGY
    • C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11D—DETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
    • C11D3/00—Other compounding ingredients of detergent compositions covered in group C11D1/00
    • C11D3/16—Organic compounds
    • C11D3/37—Polymers
    • C11D3/3746—Macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds
    • C11D3/3757—(Co)polymerised carboxylic acids, -anhydrides, -esters in solid and liquid compositions
    • C11D3/3761—(Co)polymerised carboxylic acids, -anhydrides, -esters in solid and liquid compositions in solid compositions

Definitions

  • the invention relates to a process for the production of zeolite granules with a high bulk density, which have a pronounced adsorption capacity for liquid active substances, and the use of the zeolite granules as a preliminary product for the production of detergents and cleaning agents.
  • European patent application 21 267 discloses granules containing zeolites and alkali silicates which have a particle size between 0.15 and 2 mm and a bulk density of 300 to 700 g / l. They are also suitable for adsorbing liquid detergent components, in particular nonionic surfactants. To prepare them, a dry premix of zeolite and alkali metal silicate (mixing ratio 1: 1 to 1: 8) is sprayed with water and agglomerated in a granulator, whereupon the excess water is dried to a residual proportion of less than 5% by weight Will get removed.
  • the bulk density of the relatively fine-particle spray products is in the range from 450 to 600 g / 1, the size of the particles being between 0.05 and 0.5 mm.
  • German patent application 3838086 describes the production of granules from zeolite and the sodium or potassium salts of polymeric or copolymeric carboxylic acids, the agglomeration or granulation taking place with the addition of a granulating liquid and the agglomerate obtained until a free-flowing granulate is reached a bulk density of 750 to 1,000 g / 1 is dried.
  • This is based on a homogeneous powdery mixture of zeolite and the salt of the (co) polymeric carboxylic acids and granulated in a further mixing and granulation stage with the addition of water, which is preferably based on the powder mixture kept in motion is sprayed on.
  • the polycarboxylates are introduced in solid form and are not added in dissolved form as a constituent of the granulating liquid, since the amount of granulating liquid used is a critical factor and must therefore be metered exactly. Excessive amounts of granulating liquid lead to granules with a broad grain spectrum and an undesirably high coarse fraction (particle size above 2 mm length) and to a lower bulk density.
  • the invention relates to a process for the production of granules from zeolite and sodium or potassium salts of polymeric or copolymeric carboxylic acids, the granulation being carried out with the addition of a granulating liquid and the granules obtained having a free-flowing granulate having a bulk density of 750 to 1,000 g / 1 is dried, which is characterized in that a mixture of water, surfactants and (co) polymeric carboxylates is used as the granulating liquid, the content of surfactants in the granulating liquid being at least 10% by weight.
  • zeolites are those of the zeolite A type. Mixtures of zeolite NaA and NaX can also be used, the proportion of zeolite NaX in such mixtures advantageously being less than 30%.
  • Preferred zeolites have no particles larger than 30 ⁇ m, consist of at least 80% particles smaller than 10 ⁇ m and are of detergent quality.
  • zeolite powder in addition to zeolite powder as such, spray-dried zeolite powder mixtures (products from Degussa, trade name Wessalith), the small amounts of additives such as sodium sulfate, salts of nitrilotriacetic acid, sodium hydroxide, carboxymethyl cellulose, (co) polymeric carboxylates or contain nonionic surfactants.
  • part of the zeolite is used in the form of a 45 to 55% by weight aqueous suspension.
  • 5 to 30% by weight of zeolite, based on the total amount of zeolite are introduced as an aqueous suspension and 95 to 70% by weight, based on the total amount of zeolite, as a powder.
  • the zeolite suspensions used usually contain about 1.5 to 3% by weight, based on the suspension, of stabilizers, which also include nonionic surfactants, anionic surfactants or polymeric polycarboxylates. However, the proportion of these active ingredients introduced via the suspension is so small that the effect according to the invention can only be achieved by using additional amounts of surfactants and (co) polymeric carboxylates.
  • the granules which are produced by the process according to the invention preferably contain 50 to 95% by weight, in particular 70 to 92% by weight, based on the dried granules, of water-containing zeolite.
  • Suitable water-soluble salts of the homopolymeric and / or copolymeric carboxylic acids contained in the granules, of which the sodium salts are preferred are polyacrylic acid, polyethacrylic acid and polymaleic acid, copolymers of acrylic acid or methacrylic acid with maleic acid or vinyl ethers such as vinyl methyl ether or Vinyl ethyl ether, also with vinyl esters such as vinyl acetate or vinyl propionate, acrylic id, methacrylamide and with ethylene, propylene or styrene.
  • the proportion thereof in the interest of sufficient water solubility is not more than 50 mol%, preferably less than 30 mol%.
  • Copolymers of acrylic acid and methacrylic acid with maleic acid have proven to be particularly suitable. Copolymers containing 50 to 90% by weight of acrylic acid and 50 to 10% by weight of maleic acid are particularly preferred.
  • the relative molecular weight of the homo- or copolymeric polycarboxylates is generally 2,000 to 150,000, preferably 5,000 to 100,000.
  • the polycarboxylates are preferably 30 to 50% by weight, in particular 35 to 45% by weight, in aqueous form Solutions used.
  • water-soluble inorganic salts for example sodium sulfate, can be added to these solutions in amounts of up to 10% by weight, based on the polycarboxylate used.
  • the polycarboxylates are initially presented in powder form together with the finely divided zeolite. It is preferred to use a maximum of 50% by weight and in particular a maximum of 40% by weight of the polymeric carboxylates in powder form.
  • the commercially available salts of (co) polymeric carboxylic acids in powder form often contain 5 to 15% by weight of moisture. This proportion of water is also included in the calculation of the water balance.
  • the proportion of the salts in the preparation of the compositions or in the composition of the finished granules is based on anhydrous salt.
  • the granules according to the invention preferably contain the salts of the polymeric or copolymeric carboxylic acids in amounts of 2 to 12% by weight and in particular in amounts of 4 to 10% by weight.
  • the granulating liquid contains at least water as a liquid component, at least polymeric or copolymeric carboxylates as a solid component and anionic and / or nonionic surfactants.
  • the granulating liquid preferably contains a mixture of water and liquid nonionic surfactants as the liquid constituent.
  • the granulating liquid advantageously consists of 5 to 30% by weight of (co) polymeric carboxylate, 10 to 75% by weight of anionic and / or nonionic surfactants and 7 to 70% by weight of water.
  • the granulating liquid consists of 0 to 25% by weight of (co) polymeric carboxylate and 10 to 65% by weight Nonionic surfactants or 10 to 40% by weight of anionic surfactants and 10 to 68% by weight of water.
  • the liquid nonionic surfactants used are preferably ethoxylated and / or propoxylated fatty alcohols with preference for the ethoxylated fatty alcohols, in particular addition products of 2 to 7 moles of ethylene oxide (E0) with linear primary alcohols, such as, for. B. on coconut oil, tallow fat or oleyl alcohol, or on primary alcohols branched methyl-branched in the 2-position (oxo alcohols).
  • E0 ethylene oxide
  • Preferred ethoxylated fatty alcohols are furthermore those with a narrow homolog distribution (narrow ranks ethoxylates, nre).
  • the water-soluble anionic surfactants are alkali metal salts, sodium or potassium salts from the class of the sulfonates and sulfates.
  • Preferred surfactants of the sulfonate type are Cg-Ci3-alkylbenzenesulfonates, in particular Ci2-alkylbenzenesulfonate, and sulfonates based on oleochemicals, such as the esters of oc-sulfofatty acids, the sulfo group being in its salt form (mono salt), e.g. B. the oc-sulfonated methyl esters of hydrogenated coconut, palm kernel or tallow fatty acids into consideration.
  • Suitable surfactants of the sulfate type are, for example, the optionally ethoxylated sulfuric acid monoesters from primary alcohols of natural and synthetic origin, ie from fatty alcohols, such as, for example, B.
  • the solid, water-soluble anionic surfactants can be incorporated in the liquid constituents of the granulating liquid in powder form or in paste form. If aqueous surfactant pastes are used, the water content is included in the calculation of the liquid constituents, or the amount of liquid introduced into the granule stage can be reduced by this amount.
  • granulating liquid is added to 100 parts by weight of zeolite, calculated as an anhydrous substance, or to a homogeneous mixture of zeolite and optionally in the form of powder in the salt of the polymeric or copolymeric carboxylic acids that preferably 15 to 45 parts by weight, in particular 18 to 40 parts by weight, based on the moist granules, of liquid constituents are present.
  • the proportion of free water added, which is not bound as water of crystallization or in a comparable form, in the granulating liquid can be very small and depends solely on the amount and the concentration of the polymeric or copolymeric carboxylate solution used.
  • the granulating liquid preferably contains at least 2 parts by weight, for example 5 to 35 parts by weight and in particular 5 to 25 parts by weight, based on the moist granulate, of free water.
  • the granulation can be carried out continuously or continuously in conventional mixing and granulating devices.
  • B. pelletizers which consist of a horizontally arranged or inclined to the horizontal, cylindrical container, rotates in the longitudinal axis of a shaft equipped with mixing tools and conveyor blades.
  • the granulating liquid can be supplied through the spray nozzle attached in the wall or on the high shaft. If work is carried out continuously, two mixers connected in series can be used, the first mixer producing the dry or, if an aqueous zeolite suspension is used, the wet premix and in the second mixer the granulation with the addition of the surfactant and Polycarboxylate-containing granulating liquid takes place.
  • Continuous operation is also possible in a mixer, with either the powder streams and / or the powder streams and the zeolite suspension being combined and homogenized in a first mixing section, and the mixture after transport in a subsequent mixing section with the surfactant and polycarboxylate -containing granulating liquid treated and granulated becomes.
  • the granulating liquid is preferably sprayed onto the mixture kept in motion by means of nozzles. It is possible to spray a mixture of all the constituents of the granulating liquid or individual constituents one after the other, in particular the surfactant-containing constituents, before and after the addition of the polycarboxylate solution.
  • the granulation is generally carried out at normal to moderately elevated temperatures, preferably at temperatures between 20 and 40 ° C., and generally requires a time of 5 to 15 minutes.
  • the drying can be carried out by introducing hot gases in a third mixing zone, e.g. B. a fluidized bed, or after the granules have been discharged from the mixer, for example in a vibrating section, a free-fall dryer or in a thin layer on a conveyor belt. Drying in a fluidized bed is preferred, the temperature of the granules preferably being between 60 and 85 ° C. and in particular between 65 to 80 ° C. The drying is carried out until the water added in the granulation stage is removed to a proportion of less than 5% by weight, preferably less than 3% by weight, based in each case on the dried granules.
  • a third mixing zone e.g. B. a fluidized bed
  • water portions which were originally introduced with the zeolite or a (co) polymeric salt which is not used anhydrous can be removed during drying.
  • Such "over-dried" granules can have application-technical advantages, for example when added to detergents which contain moisture-sensitive active ingredients.
  • the dewatering of the zeolite should preferably not be driven below a water content of 18% by weight, based on zeolite, in order to avoid a reduction in activity.
  • the water content of the granules is expediently in a range in which the water-binding capacity of the zeolite is largely saturated, ie. H. in which the zeolite has a total water content of 19 to 22% by weight.
  • the granules preferably have a bulk density of 780 to 980 g / 1, in particular 800 to 950 g / 1. Because of their tight packing and their small pore volume, their absorption capacity for liquid or paste-like detergent components, in particular nonionic surfactants and foam inhibitors, for example paraffin oil or silicone oil, is opposed somewhat lighter carrier grains somewhat reduced, but is still 15 to a maximum of 20% by weight without appreciable impairment of the flowability of the granules. In view of the high packing density and the possibly already contained granules of non-ionic surfactants, this still surprisingly high adsorption capacity is completely sufficient for the usual fields of application, in particular for use as a mixture component in detergents and cleaning agents.
  • the granules obtained by the process according to the invention are distinguished by a grain spectrum in which the fine fraction (particle diameter less than 0.1 mm) is generally less than 10% and the coarse fraction (particle diameter greater than 2 m) is generally up to 40% .
  • the content of fine fractions is preferably less than 7% and is in particular 0 to 5%, while the content of coarse fractions is preferably 2 to 32%.
  • the coarse and fine particles are sieved.
  • the coarse fractions are ground and mixed into the product, while the fine fractions or the dust are returned to the granulation.
  • the granules disintegrate quickly and completely in cold water and do not leave any residues in the washing-up devices of washing machines, ie. H. they have a very good induction ability. This advantageous property is also noticeable after impregnation with nonionic surfactants and in a mixture with other powder detergent components.
  • the granules contain 2 to 25% by weight of surfactants and in particular 4 to 20% by weight of anionic and / or nonionic surfactants.
  • Particularly advantageous granules contain 75 to 90% by weight of zeolite which has been placed in an aqueous suspension in powder form or as a mixture of 94 to 73% by weight of powder and 6 to 27% by weight, in each case based on zeolite, 2 up to 10% by weight sodium salt of a copolymer of acrylic acid and maleic acid and 4 to 20% by weight liquid nonionic surfactants.
  • the granules contain zeolite as above, 3 to 8% by weight of sodium salt of a copoly- mers from acrylic acid and maleic acid and 6 to 11 wt .-% anionic surfactants, in particular alkylbenzenesulfonate and fatty alcohol sulfate.
  • the granules can be impregnated with liquid detergent constituents which cannot be incorporated into conventional powdery or granular detergents and cleaning agents in other ways or only with a loss of activity.
  • liquid detergent constituents which cannot be incorporated into conventional powdery or granular detergents and cleaning agents in other ways or only with a loss of activity.
  • foam inhibitors in particular paraffin hydrocarbons, silicones, silicone resins and bis-acylalkylenediamines derived from long-chain fatty acids and mixtures thereof.
  • Further adsorbable active ingredients are fatty acid alkylolamides and cationic plasticizers, such as quaternary ammonium salts containing long-chain fatty residues, and also fat-dissolving solvents such as terpenes.
  • the granules are preferably used as carrier grains for liquid nonionic surfactants and foam inhibitors.
  • Those components which are present in liquid form at room temperature or at the processing temperature between 25 ° C. and about 80 ° C., preferably up to 75 ° C., are considered to be “liquid”.
  • Suitable nonionic surfactants are alkoxylation products with 10 to 20 carbon atoms in the hydrophobic radical and 3 to 20 glycol ether groups. These include ethoxylation of alcohols vicina 'len diols, amino nen, thiols, fatty acid and fatty acids. Block polymers of ethylene oxide and propylene oxide, which are commercially available under the name Pluronic (from BASF / Wyandotte), are also suitable. Furthermore, alkyl glycosides or alkyl polyglycosides and mixtures thereof with the ethoxylation products mentioned can be used.
  • Preferred nonionic surfactants which can be adsorbed on the granules and together with them are in the form of a free-flowing mixture, are derived from alcohols having 12 to 18 carbon atoms which are saturated or olefinically unsaturated, linear or methyl-branched in the 2-position (Oxo residue).
  • Their reaction products with ethylene oxide (E0) or propylene oxide (PO) are water-soluble or water-dispersible mixtures of compounds with different degrees of alkoxylation, the following the specified number of EO or PO groups corresponds to a statistical mean.
  • ethoxylated fatty alcohols are Ci2-Ci8-coconut alcohols with 3 to 12 EO, C ⁇ 6-Ci8-tallow alcohol with 4 to 16 EO, oleyl alcohol with 4 to 12 EO as well as ethoxylation products with appropriate chain and EO distribution available from other native fatty alcohol mixtures .
  • ethoxylated oxo alcohols for example those of the composition C12-C15 with 5 to 10 EO and C14-C15 with 6 to 12 EO are suitable.
  • alkoxylates which contain EO groups and PO groups
  • Ci2-Ci8 alcohols of the formula R- (P0) a - (E0) b or R- (E0) b- (P0) c , where a is from 1 to 3, b is from 5 to 20 and c is from 1 to 10, where b is to be greater than c.
  • the application of the liquid, optionally heated additives, in particular the application of the nonionic surfactants and the foam inhibitors to the granules can be carried out by admixing, preferably spraying, the carrier material advantageously being kept in motion by suitable mixing devices. Further treatment of the granular adsorbate is not necessary. However, leaving the product to rest for several hours at high contents of applied liquid material can be expedient, since its diffusion into the interior of the grain takes some time. The treatment of the granules with the liquid additives leads to a further increase in the bulk density, which can rise to values of over 1000 g / l.
  • the grains can optionally be dusted with a finely divided powder as a powdering agent or coated on the surface.
  • a finely divided powder as a powdering agent or coated on the surface.
  • Suitable powdering agents have a grain size of 0.001 to at most 0.1 mm, preferably less than 0.05 mm and can be present in proportions of 0.03 to 3, preferably 0.05 to 2% by weight, based on the adsorbent loaded with additive.
  • finely powdered zeolites, silica airgel (Aerosil (R)), loose or colored pigments, such as titanium dioxide In general, however, such an aftertreatment is superfluous, especially since it does not improve the solution properties.
  • the detergent additives can be combined and mixed in a known manner with the granular or pulverulent detergent, for example a tower spray powder and its mixtures with other powder components, such as persalts, enzyme granules, bleach activators or defoamers.
  • the high bulk density and the favorable detergent retention of the additives according to the invention are transferred to these complex mixtures.
  • the detergents generally contain 10 to 40% by weight of the additive according to the invention.
  • the granulation was carried out in a mixing granulator consisting of a horizontally arranged cylindrical mixer with a rotating shaft rotating in the central axis and equipped with mixing elements (ploughshare mixer, Lödige type) with a capacity of 130 l and a connected one with a speed of 1200 up to 1,500 revolutions / minute operated knife mill.
  • the pulverulent constituents and, if appropriate, the aqueous zeolite suspension were placed in the mixing granulator and processed to form a homogeneous mixture.
  • the granulating liquid was sprayed in by means of nozzles over the course of 1 to 5 minutes and the mixture was granulated for a further 1 to 3 minutes with constant mixing.
  • the granules leaving the mixer were dried in a fluidized bed with hot, flowing dry gases (70 ° C.).
  • the fine fraction particle diameter less than 0.1 m
  • the coarse fraction particle diameter greater than 2 mm
  • the zeolite powder used was finely crystalline, spray-dried zeolite of the NaA type, which contained 20% by weight of bound water.
  • the aqueous zeolite suspension was 48% by weight.
  • the sodium salt of the acrylic acid-maleic acid copolymer used (Sokalan ( R ) cP5 from BASF / Germany) had a relative molecular weight of approximately 70,000 and was used as a 40% by weight solution; the amounts given relate to anhydrous substance.
  • zeolite 100 parts by weight of zeolite, based on anhydrous substance, were mixed with 44.2 parts by weight of a granulating liquid consisting of 19.8% by weight of Sokalan CP5, 50.6% by weight of Ci2-Ci8 fatty alcohol 5 EO and 29.6 wt .-% water, sprayed.
  • the granules obtained after drying contained 80.1% by weight of water-containing zeolite, which had been presented as a powder, 5.6% by weight of Sokalan CP5 and 14.3% by weight of C ⁇ 2-Ci8 fatty alcohol with 5 E0.
  • the bulk density before sieving was 900 g / l; the gross share was 5%.
  • zeolite 100 parts by weight of zeolite, based on anhydrous substance, were mixed with 42.5 parts by weight of a granulating liquid consisting of 13.3% by weight of Sokalan CP5, 62.1% by weight of Ci2-Ci8 fatty alcohol 7 E0 and 24.6 wt .-% water sprayed.
  • the granules obtained after drying contained 79.6% by weight of water-containing zeolite, which had been presented as a powder, 3.6% by weight of Sokalan CP5 and 16.8% by weight of Ci2-Ci8 fatty alcohol with 7 E0.
  • the bulk density before screening was 850 g / l; the gross share was 13.9%.
  • zeolite There were 100 parts by weight of zeolite, based on anhydrous substance, with 39 parts by weight of a granulating liquid consisting of 8.9% by weight of Sokalan CP5, 73.3% by weight of Ci2-Ci8 fatty alcohol with 7 E0 and 17.8% by weight of water, sprayed.
  • the granules obtained after drying contained 79.6% by weight of water-containing zeolite, which had been introduced as a powder, 2.2% by weight of Soka lan CP5 and 18.2% by weight of Ci2-Ci8 fatty alcohol with 7 E0.
  • the bulk density was 870 g / 1; the gross share was 2.9%.
  • zeolite 100 parts by weight of zeolite, based on anhydrous substance, were mixed with 47.5 parts by weight of a granulating liquid consisting of 22.7% by weight of Sokalan CP5, 20.5% by weight of sodium dodecylbenzenesulfonate and 56.8% by weight. % Water sprayed.
  • the granules obtained after drying contained 85.9% by weight of water-containing zeolite, which had been presented as a powder, 7.4% by weight of Sokalan CP5 and 6.7% by weight of sodium dodecylbenzenesulfonate.
  • the bulk density before sieving was 860 g / l; the gross share was 30.2%.
  • Example 6 100 parts by weight of zeolite, based on anhydrous substance, were mixed with 47.5 parts by weight of a granulating liquid consisting of 22.7% by weight of Sokalan CP5, 20.5% by weight of sodium dodecylbenzenesulfonate and
  • zeolite There were 100 parts by weight of zeolite, based on anhydrous substance, with 44 parts by weight of a granulating liquid consisting of 11.25% by weight of Sokalan CP5, 35.75% by weight of sodium dodecylbenzenesulfonate and 53% by weight of water , sprayed.
  • the granules obtained after drying contained 85.8% by weight of water-containing zeolite, which had been presented as a powder, 3.4% by weight of Soka lan CP5 and 10.8% by weight of sodium dodecylbenzenesulfonate.
  • the bulk weight was 770 g / 1; the gross share was 29.8%.
  • zeolite 100 parts by weight of zeolite, based on anhydrous substance, were mixed with 46.4 parts by weight of a granulating liquid consisting of 20.25% by weight of Sokalan CP5, 48.7% by weight of C ⁇ 2-C ⁇ 8 fatty alcohol 7 E0 and 31.05 wt .-% water, sprayed.
  • the granules obtained after drying contained 79.6% by weight of water-containing zeolite, 74.4% by weight as powder and 5.2% by weight as suspension, 6 parts by weight of Sokalan CP5 and 14, 4% by weight of C ⁇ 2-C ⁇ 8 fatty alcohol with 7 E0.
  • the bulk density before sieving was 940 g / l; the gross share was 31.1%.
  • zeolite 100 parts by weight of zeolite, based on anhydrous substance, with 42.0 parts by weight of a granulating liquid consisting of 29.5% by weight of Sokalan CP5, 22.9 parts by weight of C ⁇ 2-C ⁇ s fatty alcohol with 5 E0 and 47.6 wt .-% water, sprayed.
  • the granules obtained after drying contained 76.5% by weight of water-containing zeolite, 73.1% by weight as powder and 13.4% by weight as suspension, 7.6% by weight of Sokalan CP5 and 5.9% by weight of Ci2-C ⁇ 8 fatty alcohol with 5 E0.
  • the bulk density before sieving was 830 g / l; the gross proportion was 17.5 5'S.
  • zeolite 100 parts by weight of zeolite, based on anhydrous substance, were mixed with 41.0 parts by weight of a granulating liquid consisting of 19.5% by weight of Sokalan CP5; 31.3% by weight of C ⁇ 2-C ⁇ s fatty alcohol with 7 E0 and 49.2% by weight of water, sprayed.
  • the granules obtained after drying contained 85.5% by weight of water-containing zeolite, 62.5% by weight as powder and 23% by weight as suspension, 5.5% by weight of Sokalan CP5 and 8 ,8th % By weight C ⁇ 2-C ⁇ 8 _ fatty alcohol with 7 EO.
  • the bulk density before sieving was 840 g / l; the gross share was 24.5%.
  • the granules treated with the nonionic surfactant were free-flowing and had a perfect wash-in capacity, both as unblended powder and mixed with a powdered household detergent in a ratio of 1: 4.

Abstract

L'invention a pour but de développer un procédé de granulation pour la fabrication de granulats lourds de zéolite, dans lequel la quantité mise en oeuvre de liquide de granulation représente un moindre facteur critique, de telle sorte que des carboxylates (co-)polymères puissent être utilisés sous la forme de constituants dissous du liquide de granulation. Ce but est atteint grâce au fait qu'on utilise comme liquide de granulation un mélange d'eau, d'agents tensioactifs et de carboxylates (co-)polymères, la teneur en agents tensioactifs dans le liquide de granulation étant d'au moins 10 % en poids.
EP91920221A 1990-12-04 1991-11-25 Procede de fabrication de granulats de zeolite Expired - Lifetime EP0560802B2 (fr)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
DE4038609 1990-12-04
DE4038609A DE4038609A1 (de) 1990-12-04 1990-12-04 Verfahren zur herstellung von zeolith-granulaten
PCT/EP1991/002209 WO1992010559A1 (fr) 1990-12-04 1991-11-25 Procede de fabrication de granulats de zeolite

Publications (3)

Publication Number Publication Date
EP0560802A1 true EP0560802A1 (fr) 1993-09-22
EP0560802B1 EP0560802B1 (fr) 1995-05-10
EP0560802B2 EP0560802B2 (fr) 2002-08-28

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ID=6419545

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EP91920221A Expired - Lifetime EP0560802B2 (fr) 1990-12-04 1991-11-25 Procede de fabrication de granulats de zeolite

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US (1) US5399287A (fr)
EP (1) EP0560802B2 (fr)
JP (1) JP3167721B2 (fr)
KR (1) KR0181978B1 (fr)
AT (1) ATE122382T1 (fr)
DE (2) DE4038609A1 (fr)
ES (1) ES2071345T5 (fr)
WO (1) WO1992010559A1 (fr)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6683042B1 (en) 1998-09-29 2004-01-27 Henkel Kommanditgesellschaft Auf Aktien (Henkel Kgaa) Granulation method
RU2615506C1 (ru) * 2015-10-13 2017-04-05 Александр Адольфович Ламберов Способ гранулирования цеолита в качестве компонента синтетических моющих средств

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DE19504043C2 (de) * 1994-02-11 1998-07-09 Degussa Zeolithgranulate
DE19549411C2 (de) * 1994-02-11 1999-05-12 Degussa Zeolithgranulate
DE19515256A1 (de) * 1995-04-26 1996-10-31 Degussa Zeolithgranulat, Verfahren zu seiner Herstellung und Verwendung
DE69617035T2 (de) * 1995-09-04 2002-04-18 Unilever Plc Waschmittelzusammensetzungen und verfahren zu ihrer herstellung
KR100750190B1 (ko) * 2004-06-16 2007-08-31 요업기술원 골 수복에 효과적인 골 충전재 및 그의 제조 방법
GB0811302D0 (en) * 2008-06-20 2008-07-30 Dow Corning Shampoo compositions
JP5705525B2 (ja) * 2010-12-16 2015-04-22 花王株式会社 ゼオライト複合粒子群

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DE2652488C3 (de) * 1976-11-18 1983-03-10 Kali-Chemie Ag, 3000 Hannover Verfahren zur Herstellung von Granulaten aus Zeolithen und sauerstoffabgebenden Verbindungen
DE3316513A1 (de) * 1983-05-06 1984-11-08 Joh. A. Benckiser Gmbh, 6700 Ludwigshafen Abriebfeste granulate auf basis von alkalialuminiumsilikat
GB8329880D0 (en) * 1983-11-09 1983-12-14 Unilever Plc Particulate adjuncts
US4552681A (en) * 1983-12-10 1985-11-12 Henkel Kommanditgesellschaft Auf Aktien Granular, free-flowing detergent component and method for its production
DE3444960A1 (de) * 1984-12-10 1986-06-12 Henkel KGaA, 4000 Düsseldorf Koerniges adsorptionsmittel
GB8526999D0 (en) * 1985-11-01 1985-12-04 Unilever Plc Detergent compositions
DE3545947A1 (de) * 1985-12-23 1987-07-02 Henkel Kgaa Phosphatfreies, granulares waschmittel
DE3614779A1 (de) * 1986-05-02 1987-11-05 Henkel Kgaa Granulares, phosphatfreies wasserenthaertungsmittel
DE3838086A1 (de) * 1988-11-10 1990-05-17 Henkel Kgaa Verfahren zur herstellung zeolithhaltiger granulate hoher dichte
CA2017921C (fr) * 1989-06-09 1995-05-16 John Michael Jolicoeur Preparation de granules detergentes par voie de separation d'une pate detergente
US5205958A (en) * 1989-06-16 1993-04-27 The Clorox Company Zeolite agglomeration process and product
US5024782A (en) * 1989-06-16 1991-06-18 The Clorox Company Zeolite agglomeration process and product

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6683042B1 (en) 1998-09-29 2004-01-27 Henkel Kommanditgesellschaft Auf Aktien (Henkel Kgaa) Granulation method
RU2615506C1 (ru) * 2015-10-13 2017-04-05 Александр Адольфович Ламберов Способ гранулирования цеолита в качестве компонента синтетических моющих средств

Also Published As

Publication number Publication date
ES2071345T3 (es) 1995-06-16
EP0560802B2 (fr) 2002-08-28
JPH06503109A (ja) 1994-04-07
DE59105474D1 (de) 1995-06-14
JP3167721B2 (ja) 2001-05-21
DE4038609A1 (de) 1992-06-11
KR0181978B1 (ko) 1999-04-15
KR930703424A (ko) 1993-11-30
US5399287A (en) 1995-03-21
EP0560802B1 (fr) 1995-05-10
WO1992010559A1 (fr) 1992-06-25
ES2071345T5 (es) 2003-03-16
ATE122382T1 (de) 1995-05-15

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