EP0452016A2 - Verfahren zur Herstellung von Körnchen für Detergentzusammensetzungen - Google Patents

Verfahren zur Herstellung von Körnchen für Detergentzusammensetzungen Download PDF

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Publication number
EP0452016A2
EP0452016A2 EP91302852A EP91302852A EP0452016A2 EP 0452016 A2 EP0452016 A2 EP 0452016A2 EP 91302852 A EP91302852 A EP 91302852A EP 91302852 A EP91302852 A EP 91302852A EP 0452016 A2 EP0452016 A2 EP 0452016A2
Authority
EP
European Patent Office
Prior art keywords
granules
zeolite
smectite clay
finely divided
process according
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.)
Withdrawn
Application number
EP91302852A
Other languages
English (en)
French (fr)
Other versions
EP0452016A3 (en
Inventor
Howard Goodman
Gary Arthur Lymath
David John Stockley
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.)
Southern Clay Products Inc
Original Assignee
ECC International Ltd
Southern Clay Products Inc
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 ECC International Ltd, Southern Clay Products Inc filed Critical ECC International Ltd
Publication of EP0452016A2 publication Critical patent/EP0452016A2/de
Publication of EP0452016A3 publication Critical patent/EP0452016A3/en
Withdrawn legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11DDETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
    • C11D11/00Special methods for preparing compositions containing mixtures of detergents
    • C11D11/0082Special 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
    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11DDETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
    • C11D3/00Other compounding ingredients of detergent compositions covered in group C11D1/00
    • C11D3/02Inorganic compounds ; Elemental compounds
    • C11D3/12Water-insoluble compounds
    • C11D3/124Silicon containing, e.g. silica, silex, quartz or glass beads
    • C11D3/1246Silicates, e.g. diatomaceous earth
    • C11D3/1253Layer silicates, e.g. talcum, kaolin, clay, bentonite, smectite, montmorillonite, hectorite or attapulgite
    • C11D3/1266Layer silicates, e.g. talcum, kaolin, clay, bentonite, smectite, montmorillonite, hectorite or attapulgite in liquid compositions
    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11DDETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
    • C11D3/00Other compounding ingredients of detergent compositions covered in group C11D1/00
    • C11D3/02Inorganic compounds ; Elemental compounds
    • C11D3/12Water-insoluble compounds
    • C11D3/124Silicon containing, e.g. silica, silex, quartz or glass beads
    • C11D3/1246Silicates, e.g. diatomaceous earth
    • C11D3/128Aluminium silicates, e.g. zeolites

Definitions

  • This invention relates to a process for preparing granules for incorporation into detergent compositions and, in particular, to a process for preparing granules comprising a zeolite; and to detergent composition containing the granules produced by the process.
  • a detergent composition should be in granule form because the bulk density of a granular composition is higher than that of a finely divided powder with the result that a given weight of the composition can be packed into a smaller container when the composition is granular than when it is in powder form.
  • the granules should be free flowing and should also be resistant to crushing and abrasion so that they can withstand handling and transportation in containers. They should also be relatively white in colour and will typically have sizes in the range of from 0.75mm to 2.0mm.
  • Zeolite which is a cation exchanging aluminosilicate, is included in detergent compositions to perform the function of a builder or scavenger of metal cations, especially calcium and magnesium ions, from the washing water, which ions, if allowed to remain in solution, would impair the effectiveness of the surfactant present in the detergent composition.
  • a builder or scavenger of metal cations especially calcium and magnesium ions
  • the function of the builder in detergent compositions has been fulfilled by water-soluble condensed phosphate salts, for example sodium hexametaphosphates, but the discharge of large quantities of phosphates into rivers is damaging to the environment, and there is therefore a growing trend towards replacing phosphate builders with zeolites.
  • a zeolite with a particularly advantageous cation exchange capacity is known as zeolite A or zeolite 4A, and it is this zeolite which is commonly found in detergent compositions.
  • Zeolite A is generally available in commerce in the form of a fine powder having particles of size of the order of a few microns, but it has hitherto been found difficult to form the zeolite into granules of suitable size which are sufficiently coherent to withstand handling and transportation in packages without the use of additional binding materials which add to the expense and are undesirable in the complete detergent compositions.
  • An attempt to overcome this problem is disclosed in EP-A-0279040 in which the detergent builder is prepared by spray-drying a feed suspension containing the zeolite and bentonite.
  • a smectite clay for example bentonite, is often included in a detergent composition.
  • the clay may be included on account of its fabric softening properties, or as a stabilising agent for the detergent composition, but the use of the clay brings with it the disadvantage that the clay is somewhat dark in colour and therefore imparts an undesirable dark colouration to the composition containing it.
  • a process for preparing a granule for incorporation in a detergent composition which process comprises the steps of
  • the process of the invention preferably includes the further step of:
  • Granules prepared in accordance with the invention are solid and will comprise the smectite clay and zeolite in a weight ratio of from 1:9 to 9:1.
  • the present invention also provides a detergent composition which includes granules prepared in accordance with the process of the present invention.
  • the detergent composition will contain a surfactant and optionally other ingredients in amounts known per se .
  • the smectite clay may be montmorillonite, saponite, hectorite, nontronite or beidellite, but is most conveniently a bentonite clay which is a naturally occurring clay of volcanic origins consisting predominantly of montmorillonite.
  • the weight ratio of zeolite to smectite clay charged to the pan may preferably be in the range of from 2:8 to 8:2, more preferably 3:7 to 7:3, especially 7:3.
  • the smectite clay in its initial, finely divided, particulate form preferably has a particle size distribution such that substantially all of it passes through a No. 60 mesh British Standard sieve (nominal aperture 0.250mm).
  • the zeolite is most advantageously a synthetic zeolite such as zeolite A which has a chemical composition corresponding to the approximate formula:-
  • the initial, finely divided, particulate zeolite has a particle size distribution such that it consists predominantly of particles having sizes in the range from 1 to 10 microns.
  • the granules of the present invention may also incorporate minor proportions of other ingredients, and up to 20% of the total weight of the granules may be water (as residual water derived either from the water binder added or moisture present in either of the clay or zeolite components).
  • No additional liquid binder material is essential to form the granules; i.e. the water used in step (a) is preferably the sole liquid binder employed.
  • the size of the final granules, after sieving is preferably from 0.75mm to 2.0mm, most preferably from 0.85mm to 1.7mm. Also, the granules preferably should not contain more than about 7% by weight of particles smaller than 0.15mm.
  • the smectite clay and the zeolite are preferably tumbled together in a pan granulator.
  • the Eirich pan granulator is an example of a particularly suitable device.
  • the quantities of zeolite and smectite clay added to the pan are those necessary to give the desired proportions of each component in the resultant granules and this will normally mean that from 10 to 90% by weight of smectite clay and from 90 to 10% by weight of zeolite are added, based on the total weight of smectite clay and zeolite.
  • the water is preferably added in the form of a fine spray and in an amount such that it constitutes preferably at least 10% and preferably no more than 40% of the total weight of the granules formed in step (a) of the process.
  • smectite clay/zeolite mixture charged to the pan, from about 11 to about 67 parts by weight of water may be employed.
  • the granules may conveniently be thermally dried in step (b) in, for example, a fluidised bed dryer.
  • the process of the present invention provides granules which are sufficiently coherent to withstand handling and transportation in containers without the use of an additional binding material. It is believed that the smectite clay itself acts as a binder which makes it possible to form coherent granules containing a zeolite.
  • the granules of the invention also have the advantages of being relatively light in colour compared with the smectite clay on its own.
  • a typical, conventional detergent composition contains the following ingredients normally in amounts in the ranges given below:-
  • At least part of the Zeolite A and at least part of the smectite clay in the foregoing composition can be replaced by granules in accordance with the present invention.
  • the anionic surfactant may be, for example, an alkyl benzene sulphonate or a fatty alcohol ether sulphate.
  • the nonionic surfactant may be, for example, an alkyl polyethyleneglycol ether or a nonylphenol polyethyleneglycol ether.
  • the suds controlling agent may be, for example, a soap, a silicone oil or a paraffin.
  • the bleaching agent may be, for example, sodium perborate or sodium percarbonate.
  • the invention is illustrated by the following Example.
  • the moist granules were then dried in a fluidised bed dryer at a temperature of 80°C for a time sufficient to reduce the water content of the granules to 14% by weight.
  • the granules were then screened on a sieve having a nominal aperture size of 1.2mm and the granules passing through the sieve were retained as the product.
  • the starting materials and the product granules were tested for bulk density and for reflectance to violet light of wavelength 457nm and the results obtained are set forth in the following Table:
  • the granules were found to be sufficiently coherent to be able to withstand bulk handling and transportation in containers, and the reflectance to violet light of 457nm wavelength of 77.1% was sufficiently high to give the granules an acceptably light colour such that they would not impair the white appearance of a detergent composition in which they were incorporated.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Wood Science & Technology (AREA)
  • Organic Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Detergent Compositions (AREA)
  • Silicates, Zeolites, And Molecular Sieves (AREA)
EP19910302852 1990-04-12 1991-04-02 A process for preparing granules for detergent compositions Withdrawn EP0452016A3 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
GB909008462A GB9008462D0 (en) 1990-04-12 1990-04-12 Granules for detergent compositions
GB9008462 1990-04-12

Publications (2)

Publication Number Publication Date
EP0452016A2 true EP0452016A2 (de) 1991-10-16
EP0452016A3 EP0452016A3 (en) 1992-03-11

Family

ID=10674431

Family Applications (1)

Application Number Title Priority Date Filing Date
EP19910302852 Withdrawn EP0452016A3 (en) 1990-04-12 1991-04-02 A process for preparing granules for detergent compositions

Country Status (6)

Country Link
EP (1) EP0452016A3 (de)
JP (1) JPH04225098A (de)
AU (1) AU642230B2 (de)
CA (1) CA2040050A1 (de)
GB (2) GB9008462D0 (de)
NZ (1) NZ237774A (de)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0563631A1 (de) * 1992-03-28 1993-10-06 Hoechst Aktiengesellschaft Aus Alumosilicaten und Natriumsilicaten bestehende Cogranulate, ein Verfahren zu ihrer Herstellung und ihre Verwendung
EP0613943A1 (de) * 1993-03-03 1994-09-07 Süd-Chemie Ag Waschmittelzusatz für gewebeweichmachende Waschmittel
EP0627484A1 (de) * 1993-06-02 1994-12-07 The Procter & Gamble Company Mit feinkörnigem Material zu beschichtende Tonagglomerate
WO2001040426A1 (en) * 1999-11-29 2001-06-07 Iq Center Co., Ltd. Cleaning composition and method for preparing the same

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2297977A (en) * 1995-02-07 1996-08-21 Procter & Gamble Detergent composition containing Zeolite MAP

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE3060548D1 (en) * 1979-06-18 1982-08-05 Pq Corp Agglomerated zeolite ion exchanger
AU549122B2 (en) * 1981-02-26 1986-01-16 Colgate-Palmolive Pty. Ltd. Spray dried base beads and detergent compositions
AU549000B2 (en) * 1981-02-26 1986-01-09 Colgate-Palmolive Pty. Ltd. Base beads for detergent compositions
DE3620009A1 (de) * 1986-06-13 1987-12-17 Henkel Kgaa Koernig agglomerierte natriummetasilikat enthaltende reinigungsmittel, verfahren zu ihrer herstellung und ihrer verwendung
DE3702764A1 (de) * 1987-01-30 1988-08-11 Degussa Waschmittelbuilder

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0563631A1 (de) * 1992-03-28 1993-10-06 Hoechst Aktiengesellschaft Aus Alumosilicaten und Natriumsilicaten bestehende Cogranulate, ein Verfahren zu ihrer Herstellung und ihre Verwendung
EP0613943A1 (de) * 1993-03-03 1994-09-07 Süd-Chemie Ag Waschmittelzusatz für gewebeweichmachende Waschmittel
US5480578A (en) * 1993-03-03 1996-01-02 Sud-Chemie Ag Detergent additive for detergents containing a fabric softener
EP0627484A1 (de) * 1993-06-02 1994-12-07 The Procter & Gamble Company Mit feinkörnigem Material zu beschichtende Tonagglomerate
WO2001040426A1 (en) * 1999-11-29 2001-06-07 Iq Center Co., Ltd. Cleaning composition and method for preparing the same
US6828288B2 (en) 1999-11-29 2004-12-07 Iq Center Co., Ltd. Cleaning composition and method of preparing the same

Also Published As

Publication number Publication date
JPH04225098A (ja) 1992-08-14
GB2242909B (en) 1993-07-07
AU642230B2 (en) 1993-10-14
AU7432591A (en) 1991-10-17
EP0452016A3 (en) 1992-03-11
GB9106793D0 (en) 1991-05-22
NZ237774A (en) 1993-07-27
CA2040050A1 (en) 1991-10-13
GB9008462D0 (en) 1990-06-13
GB2242909A (en) 1991-10-16

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Withdrawal date: 19940430