EP1891191A1 - Granules de bentonite a decomposition rapide - Google Patents

Granules de bentonite a decomposition rapide

Info

Publication number
EP1891191A1
EP1891191A1 EP06742901A EP06742901A EP1891191A1 EP 1891191 A1 EP1891191 A1 EP 1891191A1 EP 06742901 A EP06742901 A EP 06742901A EP 06742901 A EP06742901 A EP 06742901A EP 1891191 A1 EP1891191 A1 EP 1891191A1
Authority
EP
European Patent Office
Prior art keywords
bentonite
granules
water
alkali metal
sodium
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.)
Granted
Application number
EP06742901A
Other languages
German (de)
English (en)
Other versions
EP1891191B1 (fr
Inventor
Ulrich Sohling
Andreas Werner
Olivier Mortaigne
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Sued Chemie AG
Original Assignee
Sued Chemie AG
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Sued Chemie AG filed Critical Sued Chemie AG
Priority to PL06742901T priority Critical patent/PL1891191T3/pl
Publication of EP1891191A1 publication Critical patent/EP1891191A1/fr
Application granted granted Critical
Publication of EP1891191B1 publication Critical patent/EP1891191B1/fr
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

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
    • C11D11/00—Special methods for preparing compositions containing mixtures of detergents
    • C11D11/0082—Special methods for preparing compositions containing mixtures of detergents one or more of the detergent ingredients being in a liquefied state, e.g. slurry, paste or melt, and the process resulting in solid detergent particles such as granules, powders or beads
    • 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
    • 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
    • C11D3/1253—Layer silicates, e.g. talcum, kaolin, clay, bentonite, smectite, montmorillonite, hectorite or attapulgite
    • C11D3/126—Layer silicates, e.g. talcum, kaolin, clay, bentonite, smectite, montmorillonite, hectorite or attapulgite in solid 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
    • C11D7/00—Compositions of detergents based essentially on non-surface-active compounds
    • C11D7/02—Inorganic compounds
    • C11D7/04—Water-soluble compounds
    • C11D7/10—Salts
    • C11D7/14—Silicates

Definitions

  • the invention relates to a process for the production of rapidly disintegrating bentonite granules and bentonite granules which can be obtained by this process.
  • Detergent formulations use bentonites to create a built-in soft-grip effect. These bentonites have a high swelling capacity, especially when activated as sodium bentonite. In the application, however, difficulties arise because on the surface of the bentonite particles on contact with water rapidly forms a gel layer, which hinders the further access of water. After a rapid initial formation of the gel layer, therefore, the decay of the bentonite granules slows down in the water, because the core of the particles remains stable for a long time and is only very slowly swollen by the penetrating water and thus decays.
  • EP 1 102 729 B1 the problem of defective disintegration of the bentonite granules is attempted to be solved by reducing the swelling capacity of the bentonite granules without disturbing the disintegration of the bentonite into individual lamellae, so that the bentonite present in the wash liquor is dissolved in the leachate considerable extent to the formation of a soft grip effect is available.
  • a bentonite having a montmorillonite content of at least 85% by weight is first dried to a moisture content of from 25 to 35% by weight. The dried bentonite is then comminuted and processed by adding water to an extrudable paste having a moisture content of 25 to 40 wt .-%.
  • This paste is then extruded through a 4 to 10 mm diameter orifice and the extrudate is dried to a moisture content of 10 to 14% by weight. After drying, the extrudates are calcined at 120 to 250 0 C until they have an ignition loss of less than 4% at 190 0 C.
  • the bentonite extrudates are then comminuted again. For the production of this bentonite with a low swelling capacity, a bentonite is already used as starting material, which after activation with sodium ions in contact with water only in relative moderately small extent swells or shows only a slight tendency to form a gel.
  • No. 4,746,445 describes bentonite agglomerates which are prepared by spraying finely divided bentonite with sodium silicate as binder.
  • the agglomerates contain 1 to 5% binder. Although they have a different bulk density, the agglomerates do not separate from the other detergent ingredients after incorporation into detergent powder because they have an irregular surface.
  • the agglomerates have an increased stability, so that they do not disintegrate in the further production steps of the detergent production. Nevertheless, they dissolve easily on contact with water.
  • a clay is used which has large proportions of montmorillonite. Particular preference is given to using a sodium bentonite.
  • the Na 2 O content of the agglomerates should be at least 0.5%, preferably at least 1%, particularly preferably at least 2%.
  • a water glass with a Na 2 OiSiO 2 module of 1: 1.6 to 1: 3.2, preferably 1: 2 to 1: 2.8 or 1: 3.0 is used for binding the bentonite agglomerates.
  • the bentonite agglomerates are prepared by spraying an aqueous solution of the binder onto finely divided bentonite while it is being agitated.
  • the binder used is a water glass solution having a solids content of 7% and a Na 2 OiSiO 2 module of about 1: 2.4. Furthermore, it is described that when using water glass solutions with another module Na 2 O: SiO 2 , which is chosen within a range of 1: 2 to 1: 3, a good agglomeration can be achieved, non-dusting agglomerates are obtained. Similar bentonite agglomerates are described in US 4,767,546, US 4,851,137, and US 4,488,972, the examples are each selected identically. The bentonite agglomerates contain 1 to 5% sodium silicate as binder.
  • a water glass solution having a solids content of from 2 to 4% by weight and a modulus of Na 2 OrSiO 2 of from 1: 2 to 1: 3 is used in each case.
  • the content of sodium oxide in the bentonite can be selected in the range of 0.5 to 10 wt .-%.
  • detailed data is not executed in the examples.
  • commercially available sodium bentonites are used.
  • exact details of the degree of activation are missing.
  • a particulate and softening coarse detergent for textiles which contains, inter alia, sodium bentonite.
  • the sodium bentonite is present as an agglomerate of smaller particles of ground sodium bentonite from which the concomitant grus has been removed after milling and before agglomeration.
  • the bentonite agglomerates are coated with a silicate or partially coated to prevent the bentonite agglomerates from sticking to surfaces. The agglomeration of the bentonite takes place with the addition of dilute sodium silicate solution.
  • Bentonitte ' ilchen which from 82.3 parts by weight of anhydrous bentonite, 16.1 parts by weight of water, 1.5 parts by weight of sodium silicate and 0.06 parts by weight of a blue dye, the is applied to the surface of the particles exist.
  • the bentonite used is a sodium carbonate-treated bentonite which, after the sodium carbonate treatment, is freed of its coagulum parts by centrifuging.
  • US 4,699,729 describes a process for preparing a detergent composition which contains a small proportion of finely divided bentonite powder.
  • the bentonite is agglomerated on the surface of a particulate granulate. meriert.
  • sodium silicate solutions having a modulus of Na 2 OiSiO 2 of from 1: 1.6 to 1: 3.2, preferably 1: 2 to 1: 3, more preferably 1: 2.35 or 1: 2.4 may be used.
  • bentonite sodium bentonite is preferably used, wherein both a natural sodium bentonite as well as a Na 2 CO 3 activated calcium bentonite can be used.
  • the bentonite has a content of Na 2 O of 0.8 to 2.8%.
  • agglomerates of bentonite and sodium sulfate which textiles can give a soft touch effect.
  • the agglomerates are prepared by agglomerating the finely divided bentonite and the sodium sulfate with the aid of a binder.
  • moisture can be used for this purpose.
  • sodium silicate as an inorganic binder, but more accurate values for amount and modulus are not specified.
  • bentonite preferably natural sodium bentonites are used. It is also possible to use calcium bentonites which have been activated with sodium carbonate.
  • Example 1 an agglomerate of finely divided sodium bentonite and sodium sulfate is prepared using water as the binder. If the resulting agglomerates are compared in their softening properties with agglomerates obtained by agglomeration of the same bentonite with dilute sodium silicate solution, the agglomerates described first have much better properties.
  • the detergent additive contains (A) from 30 to 90% by weight of a layered silicate, (B) from 1 to 40% by weight of finely crystalline, synthetic see zeolite NaA, (C) 0 to 30 wt .-% of water-soluble salts from the class of sulfates, carbonates, silicates and phosphates of sodium or potassium, and (D) the rest to 100 wt .-% water.
  • the detergent additives are free of phosphates and alkali silicates.
  • Preferred components of group (C) are sodium sulfate and sodium carbonate, both of which are used as anhydrous salts individually or in admixture.
  • the components are dry blended, then mixed with an aqueous component containing a portion of the zeolite. Granulate formation thus takes place without the addition of water glass.
  • the softener mixture contains discrete softening particles containing at least about 75% by weight of a smectite-type clay and less than about 5% by weight of anionic, nonionic, ampholytic, and zwitterionic surfactants.
  • the plasticizer particles are prepared by spraying the smectite clay with a solution containing a quaternary ammonium compound. Since there is no exchange reaction with the clay, as long as the ammonium compound is adsorbed only on the surface of the clay, the amount of the ammonium compound can be remarkably reduced.
  • the clays used are preferably sodium benzonites.
  • the plasticizer particles may optionally contain, in addition to the smectite-type clay, substances which soften the desired fabric or do not adversely affect washing, examples of suitable materials being binder or agglomerating agents, e.g. For example sodium silicate.
  • a suitable sodium silicate has a module Na 2 O: SiO 2 of, for example, 1: 2.4.
  • EP 0 387 426 A2 describes a detergent additive for producing a soft-grip effect which contains a natural hectorite of specific composition. The agglomeration of the natural hectorite is carried out in Example 1 with water as the agglomerating agent. The wet agglomerates are dried and sieved to the desired particle size.
  • sorbents which are used for example as animal litter.
  • a weakly swelling bentonite preferably a calcium bentonite, with a Montmorrilonitgehalt of about 40 to 65 wt .-% with a basic reacting alkali metal compound homogenized by intimate kneading and transferred under ion exchange in a swellable bentonite.
  • the alkali metal compound preferably the corresponding sodium compound, is used in an amount of from 0.1 to 1.5% by weight, preferably from 0.25 to 1.5% by weight, based on the dried crude bentonite.
  • the alkali metal compound among others, a water glass solution is used.
  • the added amounts correspond to a Na 2 O content of 0.5%, 1.0% and 1.5%.
  • the crude calcium bentonite is not first activated with an alkali metal compound, and then the activated bentonite is granulated.
  • water glass as a binder for the production of bentonite agglomerates, as are customary in detergent additives, has been known for some time.
  • water glasses with a Na 2 OiSiO 2 module of about 2.4 are used.
  • the water glasses must be strongly alkaline to prevent premature polymerization of the water glass. This would lead to a solidification of the granules and thus to a poor disintegration in the wash liquor.
  • the bentonite granules become detergent compositions further processed, for which the bentonite granules must first be packaged after production and then, for example, transported to the detergent producer. In the process, workers come into contact with the bentonite granules or the dust they produce. Because of the highly alkaline properties of the water glass, especially when used in higher amounts, the bentonite granules are irritating, ie when handling the bentonite granules appropriate safety precautions must be taken.
  • the invention was based on the object to provide a process for the production of bentonite granules are available, which are obtained with which bentonite granules that can be handled without major safety precautions.
  • the granules should be able to be stored for a long time and show rapid disintegration in the wash liquor.
  • alkali metal ions overactivated bentonite which is overactivated with at least 110% of its cation exchange capacity with alkali metal ions;
  • the over-activated with alkali metal ions bentonite is granulated with a water glass solution.
  • a bentonite overactivated with alkali metal ions is meant a bentonite which has been reacted with a larger amount of an alkali metal compound, for example soda or potassium oxalate, than corresponds to its cation exchange capacity.
  • the cation exchange capacity is determined on the starting material, ie the non-activated bentonite, by first exchanging the exchangeable cations for ammonium ions and then the nitrogen content of the washed and dried bentonite is determined by elemental analysis. From the found amount of exchangeable cations then the amount of alkali metal compounds to be used can be calculated.
  • the molar excess of the amount of alkali metal ions used amounts to at least 110%, preferably at least 120%, particularly preferably at least 140%, based on the cation exchange capacity of the bentonite.
  • the excess is selected in the range of 140% to 200%, more preferably in the range of 150% to 180% of the cation exchange capacity.
  • the activation of the bentonite used as starting material takes place in a manner known per se.
  • the wet bentonite which usually has a water content of 20 to 40 wt .-%, is kneaded with a suitable alkali metal compound, for example. Soda or potassium oxalate, and then dried.
  • a suitable alkali metal compound for example. Soda or potassium oxalate
  • the resulting over-activated bentonite with alkali metal ions can optionally be ground again.
  • the bentonite overactivated with alkali metal ions before granulation has a dry sieve residue on a sieve with a mesh size of 75 ⁇ m, preferably less than 15% of the weighed amount.
  • the activation can also be carried out by first slurrying the bentonite used as starting material in water and then activating it by adding a solid or dissolved in water alkali metal compound.
  • concentration of the reaction components is chosen so that an activated with alkali metal ions bentonite is obtained, which has the required overactivation.
  • a water glass solution is used, which has a modulus SiO 2 : Na 2 O of more than 3.2.
  • a water glass with a modulus SiO 2 : Na 2 O of more than 3.2 When using a water glass with a modulus SiO 2 : Na 2 O of more than 3.2, the irritant effect of the granules decreases significantly, which is why the granules are easier to transport and handle. For example, the granules no longer have to be classified as "irritating".
  • a potassium water glass solution or a sodium / potassium water glass solution having the above-mentioned modulus can be used in the same manner.
  • the modulus here is based on potassium oxide or the mixture of potassium oxide and sodium oxide, but has the abovementioned range of values.
  • the granulation preferably uses a water glass solution which has a solids content of at least 10% by weight, preferably at least 15% by weight, particularly preferably at least 30% by weight, particularly preferably at least 40% by weight, particularly preferably at least 50 % By weight.
  • the water glass solution is added in such an amount to the over-activated sodium bentonite that the bentonite granules at a water content of 8 wt .-% of alkali metal silicate, preferably sodium silicate, of less than 4.0 wt .-%, preferably less than 3, 5 wt .-%, particularly preferably less than 3.0 wt .-%, preferably less than 2.6 wt .-%, in particular less than 2.0 wt .-%.
  • alkali metal silicate preferably sodium silicate
  • the bentonite overactivated with alkali metal ions is prepared from a bentonite having a pH of more than 7, preferably a pH of more than 8, more preferably a pH of more than 9 in an aqueous slurry containing 2% by weight of bentonite , in particular has a pH in the range of 8-10.
  • the over-activated with alkali metal ions bentonite has a swelling capacity in water of at least 15 ml / 2 g. Due to the high swelling capacity of the rapid disintegration of the granules is supported. In spite of the high swelling capacity of the bentonite overactivated with alkali metal ions, no delay in the disintegration of the granules due to gelation on the bentonite grains is observed.
  • the over-activated alkali metal ion bentonite is preferably prepared by activation of a calcium bentonite.
  • a calcium bentonite Common calcium bentonites can be used.
  • Such calcium bentonites usually have cation exchange capacities in the range of 50 meq / 100 g to 120 meq / 100 g.
  • the alkali metal ions with which the bentonite is overactivated are preferably selected from the group of sodium ions and Selected potassium ions, with sodium ions being particularly preferred.
  • the bentonite used as starting material is preferably activated with a compound from the group of sodium carbonate, sodium bicarbonate, sodium phosphate, sodium oxalate and sodium citrate. Suitable sodium phosphates are, for example, trisodium monophosphate and trisodium polyphosphate.
  • the potassium compound is preferably selected from the group of potassium carbonate, potassium bicarbonate, potassium phosphate, potassium citrate and potassium oxalate.
  • the activation of the bentonite, in particular calcium bentonite is carried out in a conventional manner.
  • the bentonite which may have a moisture in the range of 20 to 40 wt .-%, is kneaded with the calculated amount of the alkali metal compound. Subsequently, the over-activated with alkali metal ions bentonite can be dried, ground and optionally sifted to adjust the desired grain size.
  • the granulation of the over-activated with alkali metal bentonite takes place per se by conventional methods.
  • the waterglass solution can be sprayed onto the agitated bentonite which has been overactivated with alkali metal ions.
  • free-fall mixers can be used, in which a curtain of falling particles of the overactivated bentonite is formed, on which the water glass solution is then sprayed.
  • the water content of the granules can be lowered, for example, by introducing heated air to the desired value.
  • the water content of the finished bentonite granules is 6 to 14 wt .-%, preferably 7 to 12 wt .-%, particularly preferably 8 to 10 wt .-%.
  • the granulation of the over-activated alkali metal ion bentonite, in particular sodium bentonite but in such a way that the overactivated bentonite is placed in a high-speed mixer and the water glass is added within a short period of time in its entirety.
  • the granulation can be carried out both in a batch process and in a continuous process.
  • a so-called Eirich mixer and for continuous granulation for example, a continuously operating ploughshare mixer, as offered for example by the company Lödige, or a ring layer mixer, such as a Lödige CB mixer, can be used.
  • Another object of the invention is a bentonite granules, as it can be obtained, for example, with the method described above.
  • Bentonitgranulat is characterized by the fact that it dissolves very quickly in water or disintegrates very quickly.
  • the bentonite granules according to the invention have the following properties:
  • a swelling volume of at least 15 ml / 2g a decomposition in water after 30 seconds of at least 80%.
  • the bentonite granules preferably have a decomposition in water after 90 seconds of at least 90%, particularly preferably of at least 95% and especially preferably of at least 99%.
  • the granulated overactivated bentonite preferably has a pH of more than 10 in an aqueous slurry containing 2% by weight of granules.
  • the invention will be explained in more detail by means of examples.
  • Nessler's reagent (Merck, Art. No. 9028); Boric acid solution, 2%; Caustic soda, 32%; 0.1 N hydrochloric acid; NaCl solution, 0.1%; KCl solution, 0.1%.
  • Detection of the ionic freedom of the wash water is performed on NH, j + ions with the sensitive Nessler's reagent.
  • the washing time can vary between 30 minutes and 3 days, depending on the key.
  • the leached NH 4 + -TOn is removed from the filter, dried at HO 0 C for 2 h, ground, sieved (63 micron sieve) and dried again at 110 0 C for 2 h. Thereafter, the NH 4 + content of the clay is determined by elemental analysis.
  • the CEC (cation exchange capacity) of the clay is conventionally determined by the NH 4 + content of the NH 4 + clay determined by elementary analysis of the N content.
  • the device Vario EL 3 of the company Elementar-Heraeus, Hanau, DE, according to the instructions of the manufacturer was used. The data are given in mval / 100 g clay (meq / 100g).
  • the water content of the products at 105 0 C is determined using the method DIN / ISO-787/2.
  • the dissolution rate of the granules is investigated by a method as described in WO 99/32591.
  • the granules are first screened with a sieve of mesh size 200 microns. 8 g of the sieved material is placed in one liter of water, which is heated to 3O 0 C and comprising 21 ° German hardness. With a paddle stirrer for 90 sec. At 800 revolutions / min, stirred. The remaining residue of the granules is sieved with a sieve of mesh size 0.2 mm and then dried at 40 0 C to constant weight. The residue is weighed and the solubility determined as the difference to the weighed-in amount of granules.
  • 105 to 115 g of the granules are placed on a sieve of mesh size 0.15 mm and sieved finely divided portions of the granules.
  • the sieve is shaken again for 15 minutes and the material which has accumulated in the drip tray is weighed again. has melted. The sum of the sieve passes results in a refractoriness number of 30 min.
  • a graduated 100 ml graduated cylinder is filled with 100 ml of distilled water or an aqueous solution of 1% soda and 2% trisodium polyphosphate.
  • 2 g of bentonite are added slowly and in portions, each about 0.1 to 0.2 g, with a spatula on the surface of the water. After a drop of added portion, the next portion is added. After the 2 g of bentonite have been added and dropped to the bottom of the graduated cylinder, the cylinder is allowed to stand for one hour at room temperature. Then the height of the swollen substance in ml / 2g is read on the graduation of the measuring cylinder.
  • the X-ray images are taken on a Philips high-resolution powder diffractometer (X '-Pert-MPD (PW3040)) equipped with a CO anode. Determination of montmorillonite content via methylene blue adsorption
  • the methylene blue value is a measure of the inner surface of the clay materials.
  • the test of the clay material is carried out in the same way as for the test bentonite. From the used amount of methylene blue solution, the inner surface of the clay material can be calculated.
  • 381 mg methylene blue / g clay correspond to a content of 100% montmorillonite according to this method.
  • the bentonite used was a natural Ca bentonite which has the following properties:
  • the swelling volume of the unactivated bentonite is 12 ml / 2 mg
  • the stoichiometrically activated bentonite increases to 20 ml / 2 g, and then again to overactivated bentonite to 15 ml / 2 g to fall off.
  • Table 5 Properties of granules which were granulated with different amounts of water glass modulus SiO 2 : Na 2 O of 3.2

Landscapes

  • Chemical & Material Sciences (AREA)
  • Wood Science & Technology (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Silicates, Zeolites, And Molecular Sieves (AREA)
  • Detergent Compositions (AREA)
  • Disintegrating Or Milling (AREA)
  • Glanulating (AREA)
  • Chemical Or Physical Treatment Of Fibers (AREA)
EP06742901A 2005-05-12 2006-05-12 Granules de bentonite a decomposition rapide Active EP1891191B1 (fr)

Priority Applications (1)

Application Number Priority Date Filing Date Title
PL06742901T PL1891191T3 (pl) 2005-05-12 2006-05-12 Granulaty bentonitowe ulegające szybkiemu rozkładowi

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE102005022075A DE102005022075A1 (de) 2005-05-12 2005-05-12 Schnell zerfallende Betonitgranulate
PCT/EP2006/004489 WO2006120011A1 (fr) 2005-05-12 2006-05-12 Granules de bentonite a decomposition rapide

Publications (2)

Publication Number Publication Date
EP1891191A1 true EP1891191A1 (fr) 2008-02-27
EP1891191B1 EP1891191B1 (fr) 2010-12-22

Family

ID=36657017

Family Applications (1)

Application Number Title Priority Date Filing Date
EP06742901A Active EP1891191B1 (fr) 2005-05-12 2006-05-12 Granules de bentonite a decomposition rapide

Country Status (11)

Country Link
EP (1) EP1891191B1 (fr)
JP (1) JP4971310B2 (fr)
CN (1) CN101175844B (fr)
AT (1) ATE492622T1 (fr)
BR (1) BRPI0608600A2 (fr)
DE (2) DE102005022075A1 (fr)
ES (1) ES2358212T3 (fr)
MX (1) MX2007013874A (fr)
PL (1) PL1891191T3 (fr)
WO (1) WO2006120011A1 (fr)
ZA (1) ZA200709019B (fr)

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008290923A (ja) * 2007-05-28 2008-12-04 Kurosaki Hakudo Kogyo Kk 水分散性強化型改質ベントナイト及びその製造方法
US20150291477A1 (en) * 2012-09-28 2015-10-15 Korea Institute Of Energy Research Method for preparing granulated bentonite formed body and granulated bentonite formed body prepared thereby
KR101348134B1 (ko) 2012-09-28 2014-01-07 한국에너지기술연구원 그래뉼화 된 벤토나이트 성형체의 제조방법 및 이에 따라 제조된 그래뉼화 된 벤토나이트 성형체의 제조방법
CN108004054B (zh) * 2017-12-20 2020-04-14 苏州国建慧投矿物新材料有限公司 一种用于洗衣粉的柔顺功能粒子及其制备方法
CN111024884B (zh) * 2019-12-02 2022-04-22 武汉科技大学 一种用于冶金球团粘结剂的膨润土质量检测评价方法
NL2032305B1 (nl) * 2022-06-28 2024-01-16 Trisoplast Int B V Geconsolideerd droog mengsel dat granulair materiaal en bentoniet

Family Cites Families (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS58117294A (ja) * 1981-12-30 1983-07-12 ライオン株式会社 芳香性洗剤組成物
EP0087001B2 (fr) * 1982-02-19 1995-01-11 Laporte Industries Limited Procédé pour la fabrication des substances absorbantes
US4746445A (en) * 1982-04-08 1988-05-24 Colgate-Palmolive Company Process for manufacturing bentonite agglomerates
DE3311368A1 (de) * 1982-04-08 1983-10-27 Colgate-Palmolive Co., 10022 New York, N.Y. Teilchenfoermiges, bleichendes und weichmachendes textilwaschmittel
US4767546A (en) * 1982-04-08 1988-08-30 Colgate-Palmolive Co. Fabric softening bentonite agglomerates for use in laundry detergents
DE3311568C2 (de) * 1982-04-08 1994-10-20 Colgate Palmolive Co Teilchenförmiges und weichmachendes Grobwaschmittel, Verfahren zu dessen Herstellung und als Zusatz für Grobwaschmittel geeignetes Bentonit-Agglomerat
US4536316A (en) * 1983-06-01 1985-08-20 Colgate-Palmolive Co. Fabric softening composition containing surface modified clay
US4609473A (en) * 1984-11-26 1986-09-02 Colgate Palmolive Company Bentonite-sulfate fabric softening particulate agglomerate, processes for manufacture and use thereof, and detergent compositions containing it
JPS63150390A (ja) * 1986-12-15 1988-06-23 株式会社豊田中央研究所 洗剤組成物
US4997695A (en) * 1988-11-21 1991-03-05 James Clem Corporation Clay mixture having contamination resistance
DE3908628A1 (de) * 1989-03-16 1990-09-20 Manfred Dr Ing Braun Brikettierung von tonmehlgemengen mit zusaetzen auf walzenpressen mit formmulden und verarbeitung dieser briketts zur errichtung von wasserdichten sperrschichten
DE4243389A1 (de) * 1992-12-21 1994-06-23 Sued Chemie Ag Verfahren zur Herstellung von Sorptionsmitteln zur Aufnahme von Flüssigkeiten
CN1061946C (zh) * 1997-03-31 2001-02-14 孙忠 一种用钙基膨润土生产钠基膨润土的方法
DE19943551A1 (de) * 1999-09-11 2001-03-15 Clariant Gmbh Schwerlösliches Alkalisilikat
DE10121051A1 (de) * 2001-04-28 2002-10-31 Clariant Gmbh Builder-Zusammensetzung
CN1155515C (zh) * 2002-04-16 2004-06-30 张兴华 颗粒膨润土的生产方法
JP2004073053A (ja) * 2002-08-14 2004-03-11 Kurosaki Hakudo Kogyo Kk ペット用トイレ砂

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
See references of WO2006120011A1 *

Also Published As

Publication number Publication date
DE502006008561D1 (de) 2011-02-03
ZA200709019B (en) 2009-02-25
DE102005022075A1 (de) 2006-11-16
EP1891191B1 (fr) 2010-12-22
PL1891191T3 (pl) 2011-07-29
CN101175844A (zh) 2008-05-07
BRPI0608600A2 (pt) 2010-01-19
WO2006120011A1 (fr) 2006-11-16
MX2007013874A (es) 2008-01-28
CN101175844B (zh) 2010-06-09
JP2008540749A (ja) 2008-11-20
JP4971310B2 (ja) 2012-07-11
ATE492622T1 (de) 2011-01-15
ES2358212T3 (es) 2011-05-06

Similar Documents

Publication Publication Date Title
DE2652409C2 (de) Verfahren zur Herstellung von Waschmittelverstärkern
EP1891191B1 (fr) Granules de bentonite a decomposition rapide
EP1871862A2 (fr) Granules en mineraux naturels presentant des couches et procede de fabrication associe
DE69423542T2 (de) Synthetisiertes, anorganisches Ionenaustauschermaterial sowie dieses enthaltende Waschmittelzusammensetzung
DE69020963T2 (de) Zeolith-Agglomerierverfahren und -Produkt.
EP1904588B1 (fr) Barbotines de silicate en feuillets a haute teneur en solides
EP0753568B1 (fr) Adjuvant sous forme de granulé pour les compositions détergentes
DE3509661C2 (de) Verfahren zur Herstellung eines körnigen, Natriumtriphosphat enthaltenden Produktes
EP0613943B1 (fr) Additif pour détérgent pour agents de lavage adoucissant pour textile
EP0006618B1 (fr) Utilisation de granules d'aluminosilicates comme échangeurs de cations
EP2057257B1 (fr) Additif pour détergent à base de minéraux argileux et de copolymères contenant de la pvp
WO1991009101A1 (fr) Procede de production d'un additif adoucissant granule pour produits de lavage
DE102004060587A1 (de) Bentonite zur Störstoffbindung in der Papierherstellung
EP0970918B1 (fr) Disilicate de sodium cristallin finement divisé
EP0903401B1 (fr) Additif antimicrobien pour détergents
EP1257628B1 (fr) Agglomeres contenant du mineral en feuillets et des tensioactifs non ioniques
EP0716682B1 (fr) Adjuvant de lavage pour produits de lavage ou de nettoyage
EP0273334A1 (fr) Procédé pour la production de concentrés de peracides s'écoulant librement, stable à partir de granulation à rendre compact
DE19925928A1 (de) Feinteiliges kristallines Natriumsilikat
EP0563631B1 (fr) Cogranulés de silicate de sodium et d'aluminosilicates, procédé pour les fabriquer et utilisation de ceux-ci
EP0048435B1 (fr) Procédé de préparation de phosphates condensés granuleux
DE3035820A1 (de) Verfahren zur herstellung von granulierten alkalidi- oder -triphosphaten
DE102013010766A1 (de) Verfahren zur Herstellung von Granulaten enthaltend Kaliumchlorid und Magnesiumsulfat-Hydrat
EP0768276A1 (fr) Procédé de préparation de disilicate de sodium ayant une capacité élevée d'échange d'ion

Legal Events

Date Code Title Description
PUAI Public reference made under article 153(3) epc to a published international application that has entered the european phase

Free format text: ORIGINAL CODE: 0009012

17P Request for examination filed

Effective date: 20071203

AK Designated contracting states

Kind code of ref document: A1

Designated state(s): AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HU IE IS IT LI LT LU LV MC NL PL PT RO SE SI SK TR

RIN1 Information on inventor provided before grant (corrected)

Inventor name: MORTAIGNE, OLIVIER

Inventor name: SOHLING, ULRICH

Inventor name: WERNER, ANDREAS

DAX Request for extension of the european patent (deleted)
17Q First examination report despatched

Effective date: 20100208

GRAP Despatch of communication of intention to grant a patent

Free format text: ORIGINAL CODE: EPIDOSNIGR1

GRAS Grant fee paid

Free format text: ORIGINAL CODE: EPIDOSNIGR3

GRAA (expected) grant

Free format text: ORIGINAL CODE: 0009210

AK Designated contracting states

Kind code of ref document: B1

Designated state(s): AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HU IE IS IT LI LT LU LV MC NL PL PT RO SE SI SK TR

REG Reference to a national code

Ref country code: GB

Ref legal event code: FG4D

Free format text: NOT ENGLISH

REG Reference to a national code

Ref country code: CH

Ref legal event code: EP

REG Reference to a national code

Ref country code: IE

Ref legal event code: FG4D

REF Corresponds to:

Ref document number: 502006008561

Country of ref document: DE

Date of ref document: 20110203

Kind code of ref document: P

REG Reference to a national code

Ref country code: DE

Ref legal event code: R096

Ref document number: 502006008561

Country of ref document: DE

Effective date: 20110203

REG Reference to a national code

Ref country code: RO

Ref legal event code: EPE

REG Reference to a national code

Ref country code: NL

Ref legal event code: VDEP

Effective date: 20101222

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: LT

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20101222

REG Reference to a national code

Ref country code: ES

Ref legal event code: FG2A

Ref document number: 2358212

Country of ref document: ES

Kind code of ref document: T3

Effective date: 20110425

LTIE Lt: invalidation of european patent or patent extension

Effective date: 20101222

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: SI

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20101222

Ref country code: SE

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20101222

Ref country code: LV

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20101222

Ref country code: BG

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20110322

Ref country code: CY

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20101222

Ref country code: FI

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20101222

REG Reference to a national code

Ref country code: IE

Ref legal event code: FD4D

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: IS

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20110422

Ref country code: PT

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20110422

Ref country code: EE

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20101222

Ref country code: GR

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20110323

Ref country code: CZ

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20101222

REG Reference to a national code

Ref country code: PL

Ref legal event code: T3

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: SK

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20101222

Ref country code: NL

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20101222

PLBE No opposition filed within time limit

Free format text: ORIGINAL CODE: 0009261

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: NO OPPOSITION FILED WITHIN TIME LIMIT

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: DK

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20101222

Ref country code: IE

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20101222

26N No opposition filed

Effective date: 20110923

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: MC

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20110531

REG Reference to a national code

Ref country code: CH

Ref legal event code: PL

REG Reference to a national code

Ref country code: DE

Ref legal event code: R097

Ref document number: 502006008561

Country of ref document: DE

Effective date: 20110923

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: LI

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20110531

Ref country code: CH

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20110531

REG Reference to a national code

Ref country code: GB

Ref legal event code: 732E

Free format text: REGISTERED BETWEEN 20120802 AND 20120808

REG Reference to a national code

Ref country code: ES

Ref legal event code: PC2A

Owner name: SUD-CHEMIE IP GMBH & CO.KG

Effective date: 20121002

Ref country code: AT

Ref legal event code: PC

Ref document number: 492622

Country of ref document: AT

Kind code of ref document: T

Owner name: SUED-CHEMIE IP GMBH & CO. KG, DE

Effective date: 20120904

REG Reference to a national code

Ref country code: DE

Ref legal event code: R082

Ref document number: 502006008561

Country of ref document: DE

Representative=s name: PATENTANWAELTE STOLMAR & PARTNER, DE

Effective date: 20121025

Ref country code: DE

Ref legal event code: R082

Ref document number: 502006008561

Country of ref document: DE

Effective date: 20121025

Ref country code: DE

Ref legal event code: R082

Ref document number: 502006008561

Country of ref document: DE

Representative=s name: STOLMAR & PARTNER, DE

Effective date: 20121025

Ref country code: DE

Ref legal event code: R081

Ref document number: 502006008561

Country of ref document: DE

Owner name: SUED-CHEMIE IP GMBH & CO. KG, DE

Free format text: FORMER OWNER: SUED-CHEMIE AG, 80333 MUENCHEN, DE

Effective date: 20121025

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: LU

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20110512

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: HU

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20101222

REG Reference to a national code

Ref country code: DE

Ref legal event code: R082

Ref document number: 502006008561

Country of ref document: DE

REG Reference to a national code

Ref country code: FR

Ref legal event code: PLFP

Year of fee payment: 10

REG Reference to a national code

Ref country code: FR

Ref legal event code: PLFP

Year of fee payment: 11

REG Reference to a national code

Ref country code: FR

Ref legal event code: PLFP

Year of fee payment: 12

REG Reference to a national code

Ref country code: FR

Ref legal event code: PLFP

Year of fee payment: 13

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: IT

Payment date: 20190524

Year of fee payment: 14

Ref country code: PL

Payment date: 20190507

Year of fee payment: 14

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: BE

Payment date: 20190527

Year of fee payment: 14

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: AT

Payment date: 20190528

Year of fee payment: 14

REG Reference to a national code

Ref country code: ES

Ref legal event code: PC2A

Owner name: CLARIANT INTERNATIONAL LTD.

Effective date: 20201023

REG Reference to a national code

Ref country code: AT

Ref legal event code: MM01

Ref document number: 492622

Country of ref document: AT

Kind code of ref document: T

Effective date: 20200512

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: AT

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20200512

REG Reference to a national code

Ref country code: BE

Ref legal event code: MM

Effective date: 20200531

REG Reference to a national code

Ref country code: DE

Ref legal event code: R081

Ref document number: 502006008561

Country of ref document: DE

Owner name: CLARIANT INTERNATIONAL LTD., CH

Free format text: FORMER OWNER: SUED-CHEMIE IP GMBH & CO. KG, 80333 MUENCHEN, DE

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: BE

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20200531

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: IT

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20200512

REG Reference to a national code

Ref country code: GB

Ref legal event code: 732E

Free format text: REGISTERED BETWEEN 20220421 AND 20220427

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: PL

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20200512

P01 Opt-out of the competence of the unified patent court (upc) registered

Effective date: 20230512

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: RO

Payment date: 20230504

Year of fee payment: 18

Ref country code: FR

Payment date: 20230523

Year of fee payment: 18

Ref country code: ES

Payment date: 20230612

Year of fee payment: 18

Ref country code: DE

Payment date: 20230530

Year of fee payment: 18

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: TR

Payment date: 20230428

Year of fee payment: 18

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: GB

Payment date: 20230523

Year of fee payment: 18