Claims
- 1. A process for preparing a non-aqueous liquid detergent composition in the form of a suspension of solid, substantially-insoluble particulate material dispersed throughout a structured, surfactant-containing liquid phase, which process comprises steps of:A) forming an aqueous slurry containing from about 45% to 94% by weight of one or more alkali metal salts of linear C10-16 alkyl benzene sulfonic acids and from about 2% to 50% by weight of one or more dissolved non-surfactant salts; B) drying the slurry formed in Step A to a solid material containing from about 0.5% to 4% by weight of water; C) adding, in particulate form, the dried solid material of Step B to an agitated liquid medium comprising one or more non-aqueous organic diluents, to thereby form a structured, surfactant-containing liquid phase; and thereafter D) subjecting the structured, surfactant-containing liquid phase formed in Step C to milling or high shear agitation at a temperature from about 20° C. to 60° C., said milling or high shear agitation being sufficient to increase the yield value of said structured, surfactant-containing liquid phase to a level within the range from 1 Pa to 8 Pa, to thereby form said non-aqueous liquid detergent composition.
- 2. A process according to claim 1 wherein additional particulate material is added to said structured surfactant-containing liquid phase either before or after Step D.
- 3. A process according to claim 2 wherein(A) the alkyl group of said alkylbenzene sulfonic acid is linear and contains from about 11 to 14 carbon atoms; (B) the non-surfactant salts are selected from akali metal sulfates, citrates, carbonates and xylene sulfonates; (C) the liquid phase comprises both a non-aqueous liquid nonionic surfactant and a non-aqueous low polarity non-surfactant solvent; and (D) said additional particulate material comprises peroxygen bleaching agents selected from percarboxylic acids and salts thereof and alkali metal perborates and percarbonates.
- 4. A process according to claim 3 wherein(A) said alkylbenzene sulfonate surfactant comprises from about 0.5% to 60% by weight of the composition; (B) said non-aqueous liquid phase comprises from about 15% to 70% by weight of the composition and utilizes an alcohol alkoxylate liquid nonionic surfactant in a ratio to non-surfactant solvent of from 3:1 to 1:3; and (C) said additional particulate material comprises from about 5% to 50% by weight of the composition.
- 5. A process according to claim 4 wherein(A) said peroxygen bleaching agent is selected from alkali metal perboratesand percarbonates and comprises from about 1% to 3 0% by weight of the composition; and (B) said additional particulate material also comprises from about 0.5% to 20% by weight of the composition of particles of a bleach activator which can react with said peroxygen bleaching agent to form a peroxy acid.
- 6. A process according to claim 5 wherein(A) said alcohol alkoxylate nonionic surfactant comprises ethoxylated materials containing from about 8 to 15 carbon atoms and having from about 3 to 10 ethylene oxide moieties per molecule; and (B) said non-aqueous low-polarity non-surfactant solvent is selected from i) mono, di, tri, tetra C2-C3 alkylene glycol mono C2-C6 alkyl ethers; and ii) non-vicinal alkylene glycols containing from about 4 to 8 carbon atoms.
- 7. A process according to claim 5 wherein said additional particulate material also comprises from about 2% to 20% by weight of the composition of an organic detergent builder selected from alkali metal citrates, succinates, malonates, carboxymethylsuccinates, carboxylates, polycarboxylates, polyacetylcarboxylates and fatty acid soaps.
- 8. A process according to claim 7 wherein said organic detergent builder is selected from sodium citrate and poly-acrylate/maleate co-polymers of molecular weight ranging from about 5,000 to 100,000.
- 9. A process according to claim 5 wherein said additional particulate material also comprises from about 1% to 25% by weight of the composition of an alkalinity source selected from water-soluble alkali metal carbonates, bicarbonates, borates, silicates and metasilicates.
- 10. A process according to claim 9 wherein said alkalinity source is sodium carbonate.
- 11. A process according to claim 5 wherein said additional particulate material also comprises from about 0.1% to 4% by weight of the composition of a chelating agent selected from amino carboxylates, phosphonates, amino phosphonates, polyfunctional substituted aromatic chelating agents and combinations of these chelating agents.
- 12. A process according to claim 11 wherein said chelating agent is selected from diethylene triamine pentaacetic acid, ethylene diamine disuccinic acid, dipicolinic acid and hydroxyethyldiphosphonic acid and the salts of these chelating agents.
- 13. A process according to claim 5 wherein said additional particulate material also comprises from about 0.001% to 5% by weight of the composition of enzyme prills wherein said prills range in size from about 100 to 1,000 microns, and wherein said enzyme is selected from proteases, amylases, cellulases, and lipases.
- 14. A process according to claim 5 wherein the composition prepared thereby additionally contains(A) from about 0.1% to 4% by weight of the composition of a thickening, viscosity control and/or dispersing agent selected from acrylic acid-based polymers having a molecular weight ranging from about 2,000 to 100,000; and/or (B) from about 0.01% to 5% by weight of the composition of an ethoxylated tetraethylenepentamine clay soil removal/anti-redeposition agent; and/or (C) from about 0.0001% to 2% by weight of a compatible brightener, suds suppressor, titanium dioxide, bleach catalyst, dye and/or perfume.
- 15. A process for preparing a non-aqueous liquid detergent composition in the form of a suspension of solid, substantially-insoluble particulate material dispersed throughout a structured, surfactant-containing liquid phase, which process comprises the steps of:A) forming an aqueous slurry containing from 45% to 85% by weight of sodium linear C10-14 alkyl benzene sulfonate and from about 10% to 50% by weight of one or more dissolved salts selected from sodium citrate and sodium sulfate; B) drying the slurry formed in Step A to a solid material containing from about 0.5% to 4% by weight of water; C) adding, in particulate form, the dried solid material of Step B to an agitated liquid medium comprising a combination of non-aqueous liquid nonionic surfactant and a non-aqueous, low polarity, non-surfactant solvent, to thereby form a structured, surfactant-containing liquid phase which comprises i) from about 50% to 99% by weight of the admixture of said nonionic surfactant/solvent combination; and ii) from about 0.5% to 40% by weight of the admixture of the dried solid Step B material; D) adding soluble detergent composition adjuvants selected from ancillary surfactants, dispersants, clay soil removal/antiredeposition agents and combinations thereof to the extent of from about 0.1% to 5% by weight of the admixture; E) adding insoluble detergent composition adjuvants selected from builders, alkalinity sources, chelants, thickening agents, whitening agents and combinations thereof to the extent of from about 0.1% to 50% by weight of the admixture; F) subjecting the admixture formed in Step E to milling or high shear agitation at a temperature from about 20° C. to 60° C., said milling or high shear agitation being sufficient to increase the yield value of said admixture to a level within the range from 1 Pa to 8 Pa; and thereafter G) adding to the admixture formed in Step F additional particulate material selected from peroxygen bleaching agents, peroxygen bleach activators, enzyme prills and combinations thereof; to thereby form said non-aqueous liquid detergent composition.
- 16. A process according to claim 15 wherein the composition prepared has from about 50% to 75% by weight of the composition of a liquid phase and from about 25% to 50% by weight of the composition of a solid particulate phase.
- 17. A process according to claim 16 wherein the composition prepared has a viscosity of from about 500 to 3,000 cps.
RELATED APPLICATIONS
This application claims priority to U.S. provisional patent application Ser. No. 60/020,506, filed Jun. 28, 1996.
PCT Information
Filing Document |
Filing Date |
Country |
Kind |
102e Date |
371c Date |
PCT/US97/10699 |
|
WO |
00 |
12/23/1998 |
12/23/1998 |
Publishing Document |
Publishing Date |
Country |
Kind |
WO98/00516 |
1/8/1998 |
WO |
A |
US Referenced Citations (1)
Number |
Name |
Date |
Kind |
5368767 |
Donker et al. |
Nov 1994 |
|
Foreign Referenced Citations (5)
Number |
Date |
Country |
0 510 762 A2 |
Apr 1992 |
EP |
WO 9202610 |
Feb 1992 |
WO |
WO 9209678 |
Jun 1992 |
WO |
WO 9610072 |
Apr 1996 |
WO |
WO 9700938 |
Jan 1997 |
WO |
Provisional Applications (1)
|
Number |
Date |
Country |
|
60/020506 |
Jun 1996 |
US |