WO2015112342A1 - Procédé de fabrication de compositions de détergent comprenant des polymères - Google Patents

Procédé de fabrication de compositions de détergent comprenant des polymères Download PDF

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Publication number
WO2015112342A1
WO2015112342A1 PCT/US2015/010614 US2015010614W WO2015112342A1 WO 2015112342 A1 WO2015112342 A1 WO 2015112342A1 US 2015010614 W US2015010614 W US 2015010614W WO 2015112342 A1 WO2015112342 A1 WO 2015112342A1
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WIPO (PCT)
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alkyl
process according
surfactant
detergent
emulsion
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PCT/US2015/010614
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English (en)
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Hossam Hassan Tantawy
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The Procter & Gamble Company
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Publication of WO2015112342A1 publication Critical patent/WO2015112342A1/fr

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    • 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
    • C11D3/3788—Graft polymers
    • 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 ; Methods for using cleaning compositions
    • C11D11/0082—Special methods for preparing compositions containing mixtures of detergents ; Methods for using cleaning compositions 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
    • C11D11/0088—Special methods for preparing compositions containing mixtures of detergents ; Methods for using cleaning compositions 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 the liquefied ingredients being sprayed or adsorbed onto solid particles
    • 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 ; Methods for using cleaning compositions
    • C11D11/02—Preparation in the form of powder by spray drying
    • 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
    • C11D3/40—Dyes ; Pigments
    • C11D3/42—Brightening agents ; Blueing agents

Definitions

  • the present invention is directed to compositions comprising optical brightener and polymer and to methods of making granular detergent compositions containing optical brighteners and polymer.
  • optical brightener is used in combination with an amphiphilic graft copolymer (AGP), optimal performance of the brightener results.
  • AGP amphiphilic graft copolymer
  • the present invention addresses the aforementioned needs by providing a detergent composition comprising from 0.0001 to 10 wt of an optical brightener having a ClogP from 1 to 50 and from 0.05 to 10 wt of an amphiphilic graft copolymer.
  • the invention also provides a method of making a granular detergent composition comprising the steps of: a) forming an aqueous detergent slurry; b) spray drying said aqueous detergent slurry to form a plurality of spray-dried detergent particles; c) forming an emulsion comprising a surfactant, an optical brightener having ClogP from 1 to 50 and an amphiphilic graft co-polymer; and d) adding the emulsion from step c) to at least a portion of said plurality of spray-dried detergent particles.
  • compositions or component may include additional ingredients, but only if the additional ingredients do not materially alter the basic and novel characteristics of the claimed compositions or methods.
  • Granular laundry detergents may be manufactured using a spray drying process.
  • the spray drying process typically includes spraying an aqueous slurry comprising detergent ingredients into a spray-drying tower through which hot air flows. As it falls through the tower, the aqueous slurry forms droplets, the hot air causes water to evaporate from the droplets, and a plurality of spray-dried granules is formed.
  • the resulting granules may form the finished granular detergent composition.
  • the resulting granules may be further processed (such as via agglomeration) and/or further components (such as detergent adjuncts) may be added thereto.
  • the process of the present invention can be batch, continuous, or semi-continuous.
  • an aqueous slurry is prepared using any suitable method.
  • the aqueous slurry may be prepared by mixing detergent ingredients together in a crutcher mixer.
  • the aqueous slurry preferably comprises detersive surfactant, alkalinity source, at least one additional detergent ingredient or a combination thereof.
  • the aqueous slurry may contain water at a weight percentage of from about 25 wt to about 50 wt .
  • the aqueous slurry can comprise from above 0 wt to about 30 wt detersive surfactant, preferably from about 10 wt to about 20 wt detersive surfactant.
  • Useful amounts of an alkalinity source can include from about 1 to about 20% or from about 1 to about 10% of alkalinity source by weight of the composition.
  • the aqueous slurry is transferred from the mixer preferably through at least a first pump and a second pump to a spray nozzle.
  • the aqueous slurry is transferred in a pipe.
  • the aqueous slurry is typically transferred through an intermediate storage vessel such as a drop tank, for example when the process is semi-continuous.
  • the process can be a continuous process, in which case no intermediate storage vessel is required.
  • the first pump is a low pressure pump, such as a pump that is capable of generating a pressure of from 3xl0 5 to lxlO 6 Pa
  • the second pump is a high pressure pump, such as a pump that is capable of generating a pressure of from 2xl0 6 to lxlO 7 Pa.
  • the aqueous slurry is transferred through a disintegrator, such as disintegrators supplied by Hosakawa
  • the disintegrator can be positioned before the pump, or after the pump. If two or more pumps are present, then the disintegrator can also be positioned between the pumps. Typically, the pumps, disintegrators, intermediate storage vessels, if present, are all in series configuration. However, some equipment may be in a parallel configuration.
  • a suitable spray nozzle is a Spray Systems T4 Nozzle. Gas may be injected into the aqueous slurry at any point after the crutcher mixer and prior to being spray-dried. Further detergent ingredients may also be injected into the aqueous slurry after the crutcher mixer and prior to being spray-dried. For example an liquid anionic surfactant mix may be added to the aqueous slurry after the crutcher mixer and prior to being spray-dried.
  • the aqueous slurry is sprayed through the spray nozzle into a spray-drying tower.
  • the mixture is at a temperature of from 60°C to 140°C when it is sprayed through the spray nozzle into a spray-drying tower.
  • Suitable spray-drying towers are co-current or counter- current spray-drying towers.
  • the mixture is typically sprayed at a pressure of from 6xl0 6 Pa to lxlO 7 Pa.
  • the slurry is spray-dried to form a spray-dried powder.
  • the exhaust air temperature is in the range of from 60°C to 100°C.
  • the continuous phase of the emulsion comprises the surfactant and the discrete phase comprises the amphiphilic graft co-polymer and preferably also the brightener.
  • the emulsion can be prepared via any suitable method, using any suitable equipment. A preferred method for preparing the emulsion comprises the steps;
  • a second liquid comprising the amphiphilic graft co-polymer; iii. incorporating the optical brightener into either the first or second liquid, preferably the second liquid;
  • a mixing device can be used.
  • a preferred mixing device is a high shear mixer.
  • Suitable high shear mixers can be dynamic or static mixers.
  • a suitable dynamic mixer can be a rotor-stator mixer.
  • the mixing process can be a batch or continuous process.
  • the liquids may be at a temperature of between room temperature or from 40 °C or from 55 to 65 °C as it is added to the mixer.
  • the surfactant may be at a temperature of between room temperature or 35, and 50°C as it is added to the mixer.
  • the temperature of the mixture in the mixer can be between 25, or 40 and 60°C.
  • the surfactant in the emulsion can be any surfactant, for example, non-ionic, cationic, anionic, zwitterionic or a combination thereof.
  • the surfactant in the emulsion is a non-ionic surfactant.
  • the spray-dried particles may be present in a rotary mix drum, or a batch drum or a belt conveyer.
  • the emulsion may be transferred along a pipe to a suitable means for adding the emulsion to at least a portion of said plurality of spray-dried detergent particles.
  • a suitable means of adding could be a spray nozzle.
  • the emulsion is maintained at a temperature of between 30 and 60°C, preferably between 40 and 60°C prior to addition to the spray-dried detergent particles. This temperature is preferred because at lower temperatures, the viscosity of the emulsion increases. At lower viscosities it is easier to spray the emulsion.
  • optical brightener in combination with the amphiphilic graft polymer enables better dispersion of the optical brightener as the detergent composition contacts the wash water, leading to increased performance of the optical brightener.
  • AGP(s) of use in the present invention are obtainable by grafting a polyalkylene oxide of number average molecular weight from about 2,000 to about 100,000 with vinyl acetate, which may be partially saponified, in a weight ratio of polyalkylene oxide to vinyl acetate of about 1 :0.2 to about 1 :10.
  • the vinyl acetate may, for example, be saponified to an extent of up to 15%.
  • the polyalkylene oxide may contain units of ethylene oxide, propylene oxide and/or butylene oxide. Selected embodiments comprise ethylene oxide.
  • the polyalkylene oxide has a number average molecular weight of from about 4,000 to about 50,000, and the weight ratio of polyalkylene oxide to vinyl acetate is from about 1:0.5 to about 1:6.
  • a material within this definition based on polyethylene oxide of molecular weight 6,000 (equivalent to 136 ethylene oxide units), containing approximately 3 parts by weight of vinyl acetate units per 1 part by weight of polyethylene oxide, and having itself a molecular weight of about 24,000, is commercially available from BASF as SokalanTM HP22.
  • HP22 is a preferred AGP as it provides improved grease stain removal from fabrics during the wash.
  • AGP(s) of use in the present invention as well as methods of making them are described in detail in PCT Patent Application No. WO 2007/138054. They may be present in the granular detergent compositions of the present invention at weight percentages from about 0 to about 5%, from about 0% to about 4%, or from about 0.5% to about 2%. In some embodiments, the AGP(s) is present at greater than about 1.5%. The AGP(s) are found to provide excellent hydrophobic soil suspension even in the presence of cationic coacervating polymers.
  • the AGP(s) are based on water-soluble polyalkylene oxides as a graft base and side chains formed by polymerization of a vinyl ester component. These polymers having an average of less than or equal to one graft site per 50 alkylene oxide units and mean molar masses (M W) of from about 3000 to about 100,000.
  • the optical brightener typically has a ClogP of 1 to 50 (herein, high ClogP), or 2 to 50, or 2.5 to 50, or 3 to 50 or up to 40 or 30 or 20 or up to 10.
  • ClogP is calculated using Advanced Chemistry Development Software VI 1.02 ( ⁇ 1994-2012 ACD/Labs), Advanced Chemistry Development, Inc., 8 King Street East, Suite 107, Toronto, Ontario, Canada M5C 1B5.
  • the optical brightener preferably has an extinction co-efficient at the maximum absorbance between 400 and 750nm of less than lOOOL/mol cm.
  • Preferred optical brighteners include coumarinic and benzoxazole brighteners or mixtures thereof.
  • Coumarinic optical brighteners are particularly preferred.
  • a preferred brightener is selected from coumarinic compounds of Formula I
  • R 3 is selected from the group consisting of H, C1-C4 alkyl, and C6-C10 aromatic or heteroaromatic groups which may be substituted with -F, -CI, -Br, phenyl and C1-C4 alkyl;
  • R 4 is selected from the group consisting of H, C1-C4 alkyl optionally substituted by OH or
  • each R 9 is independently selected from H, methyl, and ethyl and x is 1 to 20;
  • R 5 is H,
  • R 6 and R 8 are selected from H and C2-C4 alkylene that combine with one of more of R 7 and R 7 to form a heterocyclic ring ;
  • R 7 and R 7' are selected from the group consisting of H and organic groups that have mass less than 350 Daltons, wherein R 7 and R 7 may combine with one another to form a heterocyclic ring; and wherein the weight of the brightener is from 160 to no more than 1400 Daltons, and mixtures thereof.
  • Preferred optical brightener for use in the present invention may be selected from compounds of Formula I
  • R 3 is selected from the group consisting of H, methyl, phenyl optionally substituted with -CI or C1-C4 alkyl, preferably methyl, triazole optionally substituted with phenyl or CI - C4 alkyl, and pyrazole optionally substituted with phenyl;
  • R 4 is selected from the group consisting of H, methyl and ethyl optionally substituted by OH or (OCH 2 CHR 9 ) x OH wherein each R 9 is independently selected from H and methyl, and x is 1 to 10;
  • R 5 ,R 6 and R 8 are H;
  • R 7 and R 7' are selected from the group consisting of H and organic groups that have mass less than 350 Daltons, wherein R 7 and R 7 may combine with one another to form a heterocyclic ring, and mixtures thereof.
  • a preferred optical brightener for use in the present invention may be selected from compounds of Formula I
  • R 3 is selected from the group consisting of H, methyl, and phenyl
  • R 4 is selected from the group consisting of H and methyl
  • R 5 ,R 6 and R 8 are H
  • R 7 and R 7' are selected from the group consisting of H, CI -CI 2 branched or unbranched alkyl, and (CH 2 CHR 9 0) X H where each R 9 is independently selected from H, methyl, and ethyl and x is 1 to 20, and mixtures thereof.
  • a preferred optical brightener for use in the present invention may be selected from benzoxazole compounds of Formula II
  • index y is 1 or 2 and each R is independently selected from the group consisting of H, -F, -CI, -Br, C1-C10 alkyl optionally substituted with halo, C6-C10 aryl, C7-C10 alkaryl, -G z -
  • N(R 12 ) 2 where z is 0 or 1 and G is selected from the group consisting of C(O) and S02 and each R 12 is independently selected from H, C1-C4 alkyl and (CH 2 CHR 9 0) x H, and C1-C4 alkyl optionally substituted by OH or (OCH 2 CHR 9 ) x OH, wherein each R 9 is independently selected from H, methyl, and ethyl and x is 1 to 20; R 11 is selected from the group consisting of aromatic and heteroaromatic organic groups having no carboxylic acid or sulfonic acid groups and weighing less than 400 Daltons.
  • Preferred optical brightener for use in the present invention may be selected from compounds of Formula III
  • each index y is independently selected from 1 or 2 and each R 10 is independently selected from the group consisting of H, -F, -CI, -Br, CI -CIO alkyl optionally substituted with halo, C6-C10 aryl, C7-C10 alkaryl, -G Z -N(R ) 2 where z is 0 or 1 and G is selected from the group consisting of C(O) and S02 and each R 12 is independently selected from H, C1-C4 alkyl and (CH 2 CHR 9 0) x H, and C1-C4 alkyl optionally substituted by OH or (OCH 2 CHR 9 ) x OH, wherein each R 9 is independently selected from H, methyl, and ethyl and x is 1 to 20; Q is a divalent moiety weighing less than 400 Daltons comprising an aromatic or heteroaromatic group and preferably having no carboxylic acid or sulfonic acid groups and weighing less than 400 Daltons
  • Suitable Q groups in Formula III include, but are not limited to, 1 ,4-naphthalene, 1,7- naphthalene, 4,4-terphenylene, 2,7-dihydro[9,10]phenanthrene, 2,5-thiophene, 4-methyl-2,5- oxazole, 2,5-1,3,4-thiadiazole, 4,4'-(l,2,3-triazol-2-yl)phenyl, 2,6-thieno[3,2-b]benzothiophene, 2,4'-(l,3,4-oxadiazol-5-yl)phenyl, and mixtures thereof.
  • the optical brightener is present in the composition in an amount from lppb to 10 wt% of the composition.
  • the composition may be a pre-treatmenet composition for applying directly to an oily stain prior to an aqueous wash or rinse step or it may be provided by combining a detergent composition with water to form a wash liquor.
  • concentration may vary widely depending on the form of application.
  • the optical brightener may be present in amounts from lppb to 50ppm in a wash liquor/solution, preferably from lOOppb or 500ppb to 35ppm.
  • a pre-treat composition or detergent compostion for dilution more usually in an amount from 0.00001 to 10 wt%, or from 0.0001 or 0.01 or even from 0.05 to 5 or 2 wt% of the pre-treat or detergent composition.
  • the optical brightener may be incorporated into the detergent composition by first forming a pre-mix comprising the optical brightener, for example where the pre-mix comprises a particle or concentrated liquid for incorporation into the composition, it may be preferred that the optical brightener is present at a level of from 0.001 or even 0.01 to 10 wt% of the pre-mix.
  • Any suitable detersive surfactant is of use in the aqueous slurry.
  • Suitable detersive surfactants include, but are not limited to: anionic surfactants, non-ionic surfactants, cationic surfactants, zwitterionic surfactants, amphoteric surfactants and any mixtures thereof.
  • Preferred surfactants include anionic surfactants, cationic surfactants, non- ionic surfactants and any mixtures thereof.
  • Suitable anionic surfactants can include alkyl benzene sulphonate.
  • the anionic detersive surfactant comprises at least 50 wt%, at least 55 wt%, at least 60 wt%, at least 65 wt%, at least 70 wt%, at least 75 wt%, at least 80 wt%, at least 85 wt%, at least 90 wt%, or even at least 95 wt%, by weight of the anionic detersive surfactant, of alkyl benzene sulphonate.
  • the alkyl benzene sulphonate is preferably a linear or branched, substituted or unsubstituted, Cs-is alkyl benzene sulphonate. This is the optimal level of the Cs-is alkyl benzene sulphonate to provide a good cleaning performance.
  • the Cs-is alkyl benzene sulphonate can be a modified alkylbenzene sulphonate (MLAS) as described in more detail in WO 99/05243, WO 99/05242, WO 99/05244, WO 99/05082, WO 99/05084, WO 99/05241, WO 99/07656, WO 00/23549, and WO 00/23548.
  • MLAS modified alkylbenzene sulphonate
  • Cs-is alkyl benzene sulphonates are linear C 1 0 -13 alkylbenzene sulphonates.
  • linear Cio-13 alkylbenzene sulphonates that are obtainable by sulphonating commercially available linear alkyl benzenes (LAB);
  • suitable LAB include low 2-phenyl LAB, such as those supplied by Sasol under the trade name Isochem ® or those supplied by Petresa under the trade name Petrelab ® .
  • Other suitable LAB include high 2-phenyl LAB, such as those supplied by Sasol under the trade name Hyblene ® .
  • the anionic detersive surfactant may preferably comprise other anionic detersive surfactants.
  • a suitable anionic detersive surfactant is a non-alkoxylated anionic detersive surfactant.
  • the non-alkoxylated anionic detersive surfactant can be an alkyl sulphate, an alkyl phosphate, an alkyl phosphonate, an alkyl carboxylate or any mixture thereof.
  • the non- alkoxylated anionic surfactant can be selected from the group consisting of; C1 0 -C2 0 primary, branched-chain, linear-chain and random-chain alkyl sulphates (AS), typically having the following formula (I):
  • M is hydrogen or a cation which provides charge neutrality, preferred cations are sodium and ammonium cations, wherein x is an integer of at least 7, preferably at least 9;
  • Cio-Cis secondary (2,3) alkyl sulphates typically having the following formulae:
  • M is hydrogen or a cation which provides charge neutrality
  • preferred cations include sodium and ammonium cations, wherein x is an integer of at least 7, preferably at least 9, y is an integer of at least 8, preferably at least 9;
  • Cio-Cis alkyl carboxylates mid-chain branched alkyl sulphates as described in more detail in US 6,020,303 and US 6,060,443; methyl ester sulphonate (MES); alpha-olefin sulphonate (AOS); and mixtures thereof.
  • MES methyl ester sulphonate
  • AOS alpha-olefin sulphonate
  • anionic detersive surfactant is an alkoxylated anionic detersive surfactant.
  • the presence of an alkoxylated anionic detersive surfactant in the spray-dried powder provides good greasy soil cleaning performance, gives a good sudsing profile, and improves the hardness tolerance of the anionic detersive surfactant system.
  • the alkoxylated anionic detersive surfactant is a linear or branched, substituted or unsubstituted C12-18 alkyl alkoxylated sulphate having an average degree of alkoxylation of from 0.5 to 30, preferably from 0.5 to 10, more preferably from 0.5 to 3.
  • the alkoxylated anionic detersive surfactant is a linear or branched, substituted or unsubstituted C12- 18 alkyl ethoxylated sulphate having an average degree of ethoxylation of from 0.5 to 10, more preferably from 0.5 to 3.
  • the alkoxylated anionic detersive surfactant is a linear unsubstituted C12-18 alkyl ethoxylated sulphate having an average degree of ethoxylation of from 0.5 to 7, more preferably from 0.5 to 3.
  • the alkoxylated anionic detersive surfactant, when present with an alkyl benzene sulphonate may also increase the activity of the alkyl benzene sulphonate by making the alkyl benzene sulphonate less likely to precipitate out of solution in the presence of free calcium cations.
  • the weight ratio of the alkyl benzene sulphonate to the alkoxylated anionic detersive surfactant is in the range of from 1 : 1 to less than 5 : 1 , or to less than 3 : 1 , or to less than 1.7:1, or even less than 1.5:1.
  • This ratio gives optimal whiteness maintenance performance combined with a good hardness tolerance profile and a good sudsing profile.
  • the weight ratio of the alkyl benzene sulphonate to the alkoxylated anionic detersive surfactant is greater than 5:1, or greater than 6: 1, or greater than 7:1, or even greater than 10:1. This ratio gives optimal greasy soil cleaning performance combined with a good hardness tolerance profile, and a good sudsing profile.
  • Suitable alkoxylated anionic detersive surfactants are: Texapan LESTTM by Co gnis; Cosmacol AESTM by Sasol; BES151TM by Stephan; Empicol ESC70/UTM; and mixtures thereof.
  • the anionic detersive surfactant comprises from 0% to 10%, preferably to 8%, or to 6%, or to 4%, or to 2%, or even to 1%, by weight of the anionic detersive surfactant, of unsaturated anionic detersive surfactants such as alpha-olefin sulphonate.
  • the anionic detersive surfactant is essentially free of unsaturated anionic detersive surfactants such as alpha- olefin sulphonate.
  • By “essentially free of it is typically meant “comprises no deliberately added”. Without wishing to be bound by theory, it is believed that these levels of unsaturated anionic detersive surfactants such as alpha-olefin sulphonate ensure that the anionic detersive surfactant is bleach compatible.
  • the anionic detersive surfactant comprises from 0% to 10%, preferably to 8%, or to 6%, or to 4%, or to 2%, or even to 1%, by weight of alkyl sulphate.
  • the anionic detersive surfactant is essentially free of alkyl sulphate. Without wishing to be bound by theory, it is believed that these levels of alkyl sulphate ensure that the anionic detersive surfactant is hardness tolerant.
  • the non-ionic detersive surfactant could be an alkyl polyglucoside and/or an alkyl alkoxylated alcohol.
  • the non-ionic detersive surfactant is a linear or branched, substituted or unsubstituted C 8-18 alkyl ethoxylated alcohol having an average degree of ethoxylation of from 1 to 10, more preferably from 3 to 7.
  • Suitable alkalinity source is of use in the aqueous slurry.
  • Suitable alkalinity sources include, but are not limited to being selected from the group of: carbonate salt; silicate salt; sodium hydroxide; and mixtures thereof.
  • Exemplary alkalinity sources may be selected from the group of: sodium carbonate; sodium silicate; and mixtures thereof.
  • the additional detergent ingredient may include a builder.
  • Any suitable builder may be of use in the aqueous slurry.
  • Suitable builders include, but are not limited to those selected from the group of: zeolite builder; phosphate builder; and mixtures thereof.
  • Non-limiting examples of useful zeolite builders include: zeolite A; zeolite X; zeolite P; zeolite MAP; and combinations thereof.
  • Sodium tripolyphosphate is a non-limiting example of a useful phosphate builder.
  • the zeolite builder(s) may be present at from about 1 to about 20 % by weight of the detergent composition. It may also be especially preferred for the granular detergent composition to comprise low levels, or even be essentially free, of builder.
  • the granular detergent composition is essentially free of zeolite, preferably has no zeolite.
  • the granular detergent composition is essentially free of phosphate, preferably has no phosphate.
  • the additional detergent ingredient may include a polymer.
  • Any suitable polymer may be of use in the aqueous slurry. Suitable polymers include, but are not limited to: polymeric carboxylate; polyester soil release agent; cellulosic polymer; and mixtures thereof.
  • One preferred polymeric material is a polymeric carboxylate, such as a co-polymer of maleic acid and acrylic acid.
  • other polymers may also be suitable, such as polyamines (including the ethoxylated variants thereof), polyethylene glycol and polyesters.
  • Polymeric soil suspending aids and polymeric soil release agents are also particularly suitable.
  • cellulosic polymer such as cellulosic polymer selected from the group of: alkyl alkoxy cellulose, preferably methyl hydroxyethyl cellulose (MHEC); alkyl cellulose, preferably methyl cellulose (MC); carboxy alkyl cellulose, preferably carboxymethylcellulose (CMC); and mixtures thereof.
  • MHEC methyl hydroxyethyl cellulose
  • MC methyl cellulose
  • CMC carboxymethylcellulose
  • Polymers may be present at from about 0.5 to about 20% or from about 1 to about 10% by weight of the detergent composition.
  • Suitable detergent ingredients may be selected from the group of: chelants such as ethylene diamine disuccinic acid (EDDS); hydroxyethylene diphosphonic acid (HEDP); starch; sodium sulphate; carboxylic acids such as citric acid or salts thereof such as citrate; suds suppressor; fluorescent whitening agent; hueing agent; flocculating agent such as polyethylene oxide; and mixtures thereof.
  • chelants such as ethylene diamine disuccinic acid (EDDS); hydroxyethylene diphosphonic acid (HEDP); starch; sodium sulphate; carboxylic acids such as citric acid or salts thereof such as citrate; suds suppressor; fluorescent whitening agent; hueing agent; flocculating agent such as polyethylene oxide; and mixtures thereof.
  • the present detergent comprises masking agents and/or whiteners (e.g. Titanium dioxide), they may be present at less than about 1 wt% or less.
  • the emulsion comprises a surfactant continuous phase and an amphiphilic graft copolymer (AGP) discrete phase.
  • AGP amphiphilic graft copolymer
  • the surfactant and the AGP are immiscible with other.
  • the surfactant is water-soluble and independently the AGP is water-soluble.
  • the surfactant and the AGP are water-soluble.
  • the graft co-polymer has a viscosity of up to 4Pa.s at 55°C, or even up to 3Pa.s. The viscosity is typically measured using a rheometer at a shear of 100s "1 and a temperature of 70°C. Those skilled in the art will recognize suitable apparatus in order to measure the viscosity.
  • An exemplary method is to measure the viscosity at a shear rate of 100s "1 at temperature of 70°C, using a TA AR 2000ex, controlled stress rheometer, using a TA Instruments Peltier Concentric Cylinder Conical DIN System, hard anodized Aluminium cup and rotor, having a rotor radius of 14mm, a rotor height of 42mm, a cup radius of 15mm, and a sample volume of 19.6ml.
  • this viscosity is preferred as it allows more efficient spraying of the emulsion on the spray-dried detergent particles.
  • the ratio of surfactant to AGP can be from 1 :2 to 2: 1.
  • AGP(s) amphiphilic graft copolymer(s)
  • spray-dried powder has a consumer undesirable yellow hue.
  • the yellowing can be especially problematic in detergent matrices having high alkalinity and/or that are processed under high temperature conditions.
  • discoloration of the granules results from the occurrence of one or more chemical reactions with the AGP(s) as it is subjected to the conditions in the tower. Such reactions may include:
  • Chain degradation reaction through oxidation may occur at the level of the polymer PEG backbone
  • Hydrolysis reactions may occur at the vinyl acetate functionalities of the hydrophobic side chains;
  • Residuals may form acetaldehyde & acetate.
  • the surfactant can be selected from non-ionic, cationic, anionic, zwitterionic surfactants and mixtures thereof.
  • the surfactant may be a non-ionic surfactant, an anionic surfactant or a mixture thereof.
  • the surfactant may be a non-ionic surfactant, or even an alkoxylated non-ionic surfactant.
  • the surfactant is anhydrous. This has the benefit of limiting the amount of water that is transferred onto the spray-dried detergent particles. It is most preferred to use a non-ionic anhydrous surfactant as this as a lower viscosity as compared to other anhydrous surfactants.
  • the non-ionic surfactant for use in the emulsion could be an alkyl polyglucoside and/or an alkyl alkoxylated alcohol.
  • the non-ionic surfactant is a linear or branched, substituted or unsubstituted C 8-18 alkyl ethoxylated alcohol having an average degree of ethoxylation of from 1 to 10, more preferably from 3 to 7.
  • Suitable non-ionic surfactants include alkyl polyglucoside and/or an alkyl alkoxylated alcohol.
  • Preferred non-ionic alkyl alkoxylated alcohols include C 8-18 alkyl alkoxylated alcohol, preferably a C 8-18 alkyl ethoxylated alcohol, preferably the alkyl alkoxylated alcohol has an average degree of alkoxylation of from 1 to 50, preferably from 1 to 30, or from 1 to 20, or from 1 to 10, preferably the alkyl alkoxylated alcohol is a C 8-18 alkyl ethoxylated alcohol having an average degree of ethoxylation of from 1 to 10, preferably from 1 to 7, more preferably from 1 to 5 and most preferably from 3 to 7.
  • the alkyl alkoxylated alcohol can be linear or branched, and substituted or un-substituted.
  • Suitable non-ionic surfactants can be selected from the group consisting of: Cs-Cis alkyl ethoxylates, such as, NEODOL® non-ionic surfactants from Shell; C 6 -Ci2 alkyl phenol alkoxylates wherein preferably the alkoxylate units are ethyleneoxy units, propyleneoxy units or a mixture thereof; C 12 -C 18 alcohol and C 6 -Ci2 alkyl phenol condensates with ethylene oxide/propylene oxide block polymers such as Pluronic® from BASF; C14-C22 mid-chain branched alcohols; C14-C22 mid-chain branched alkyl alkoxylates, preferably having an average degree of alkoxylation of from 1 to 30; alkylpolysaccharides, preferably
  • alky lpoly glycosides polyhydroxy fatty acid amides
  • ether capped poly(oxyalkylated) alcohol surfactants and mixtures thereof.
  • Anionic surfactants can include sulphate and sulphonate surfactants.
  • Preferred sulphonate surfactants include alkyl benzene sulphonate, preferably C 1 0 -13 alkyl benzene sulphonate.
  • Suitable alkyl benzene sulphonate is obtainable, preferably obtained, by sulphonating commercially available linear alkyl benzene (LAB); suitable LAB includes low 2-phenyl LAB, such as those supplied by Sasol under the tradename Isochem® or those supplied by Petresa under the tradename Petrelab®, other suitable LAB include high 2-phenyl LAB, such as those supplied by Sasol under the tradename Hyblene®.
  • a suitable anionic surfactant is alkyl benzene sulphonate that is obtained by DETAL catalyzed process, although other synthesis routes, such as HF, may also be suitable.
  • Preferred sulphate surfactants include alkyl sulphate, preferably Cs- 18 alkyl sulphate, or predominantly C 12 alkyl sulphate.
  • Another preferred sulphate surfactant is alkyl alkoxylated sulphate, preferably alkyl ethoxylated sulphate, preferably a C 8-18 alkyl alkoxylated sulphate, preferably a C 8-18 alkyl ethoxylated sulphate, preferably the alkyl alkoxylated sulphate has an average degree of alkoxylation of from 0.5 to 20, preferably from 0.5 to 10, preferably the alkyl alkoxylated sulphate is a C 8-18 alkyl ethoxylated sulphate having an average degree of ethoxylation of from 0.5 to 10, preferably from 0.5 to 7, more preferably from 0.5 to 5 and most preferably from 0.5 to 3.
  • Suitable organic anionic surfactants include alkyl aryl sulphonates, for example sodium dodecyl benzene sulphonate, long chain (fatty) alcohol sulphates, olefin sulphates and sulphonates, sulphated monoglycerides, sulphated esters, sulphonated or sulphated ethoxylate alcohols, sulphosuccinates, alkane sulphonates, alkali metal soaps of higher fatty acids, phosphate esters, alkyl isethionates, alkyl taurates and/or alkyl sarcosinates.
  • alkyl aryl sulphonates for example sodium dodecyl benzene sulphonate, long chain (fatty) alcohol sulphates, olefin sulphates and sulphonates, sulphated monoglycerides, sulphated esters, sulphonated or sulphated e
  • Suitable cationic surfactants include alkyl pyridinium compounds, alkyl quaternary ammonium compounds, alkyl quaternary phosphonium compounds, alkyl ternary sulphonium compounds, and mixtures thereof.
  • Preferred cationic surfactants are quaternary ammonium compounds having the general formula:
  • R is a linear or branched, substituted or unsubstituted C 6 -i8 alkyl or alkenyl moiety
  • Ri and R 2 are independently selected from methyl or ethyl moieties
  • R3 is a hydroxyl, hydroxymethyl or a hydroxyethyl moiety
  • X is an anion which provides charge neutrality
  • preferred anions include: halides, preferably chloride; sulphate; and sulphonate.
  • Preferred cationic detersive surfactants are mono-C6-is alkyl mono-hydroxyethyl di-methyl quaternary ammonium chlorides.
  • Highly preferred cationic detersive surfactants are mono-Cs-io alkyl mono- hydroxyethyl di-methyl quaternary ammonium chloride, mono-Cio-i 2 alkyl mono-hydroxyethyl di-methyl quaternary ammonium chloride and mono-Cio alkyl mono-hydroxyethyl di-methyl quaternary ammonium chloride.
  • a cationic surfactant can for example be an alkylamine salt, a quaternary ammonium salt, a sulphonium salt or a phosphonium salt.
  • a zwitterionic (amphoteric) surfactant can for example be an imidazoline compound, an alkylaminoacid salt or a betaine.
  • the Detergent Composition is suitable for any laundry detergent application, for example: laundry, including automatic washing machine laundering and hand laundering, and even bleach and laundry additives.
  • the detergent composition can be a fully formulated detergent product, such as a fully formulated laundry detergent product, or it can be combined with other particles to form a fully formulated detergent product, such as a fully formulated laundry detergent product.
  • the detergent composition is a granular detergent composition it may be combined with other particles such as: enzyme particles; perfume particles including agglomerates or extrudates of perfume microcapsules, and perfume encapsulates such as starch encapsulated perfume accord particles; surfactant particles, such as non-ionic detersive surfactant particles including agglomerates or extrudates, anionic detersive surfactant particles including agglomerates and extrudates, and cationic detersive surfactant particles including agglomerates and extrudates; polymer particles including soil release polymer particles, cellulosic polymer particles; buffer particles including carbonate salt and/or silicate salt particles, preferably a particle comprising carbonate salt and silicate salt such as a sodium carbonate and sodium silicate co-particle,
  • bleach catalyst particles such as transition metal catalyst bleach particles, and imine bleach boosting particles; performed peracid particles; hueing dye particles; and any mixture thereof.
  • the granular detergent composotion may also be especially preferred for the granular detergent composotion to comprise low levels, or even be essentially free, of builder. By essentially free of it is typically meant herein to mean: “comprises no deliberately added”. In a preferred embodiment, the granular detergent composition comprises no builder.
  • the whiteness of the granular detergent composition can be measured using a HunterLab Color difference meter and following appropriate operating procedure.
  • Various models of the HunterLab Color difference meter can be used, such as the HunterLab LabScan XE or HunterLab Model D25. Care is taken to make sure that the powder sample is free of lumps and is representative of the overall particle size. The readings are taken at ambient temperature.
  • a HunterLab color difference meter is used to characterize color of a sample into three different parameters according to the Hunter L, a, b color scale. In this scale, the differences between points plotted in a color space correspond to visual differences between the colors plotted.
  • the Hunter L, a, b color scale is organized in cube form. The L axis of the cube runs from top to bottom. The maximum for L is 100, which would be a perfect reflecting diffuser. The minimum for L would be zero, which would be black.
  • the a and b axes of the cube have no specific numerical limits. Positive a is red. Negative a is green. Positive b is yellow. Negative b is blue.
  • the "L-3b" (L minus 3b) value signifies the whiteness of the sample.
  • the whiteness of a blown powder according to the present invention is at least about 73.5.
  • the granular detergent composition according to the present invention may have a bulk density of from about 250 to about 550 grams per liter, or from about 300 to about 450 grams per liter.
  • the granular detergent composition may have a mean particle granule size of from about 300 to about 550 microns, or from about 350 to about 450 microns.
  • a granular laundry detergent composition according to the present invention is prepared.
  • An aqueous alkaline slurry composed of sodium sulphate, sodium carbonate, water, acrylate/maleate co-polymer and miscellaneous ingredients is prepared at 80 °C in a crutcher making vessel.
  • the aqueous slurry is essentially free from zeolite builder and essentially free from phosphate builder.
  • Alkyl benzene sulphonic acid (HLAS) and sodium hydroxide are added to the aqueous slurry and the slurry is pumped through a standard spray system pressure nozzle and atomized into a counter current spray drying tower at an air inlet temperature of 275 °C.
  • the atomized slurry is dried to produce a solid mixture, which is then cooled and sieved to remove oversize material (> 1.8mm) to form a spray-dried powder.
  • composition of the spray-dried powder is given Table 1.
  • Miscellaneous such as magnesium sulphate, and 2.1 one or more stabilizers
  • Spray-dried powder (described above in table 1) 59.38
  • Amylase (21.55mg active/g) 0.33
  • Ethoxylated C 12 -C 18 alcohol having an average degree of 1.33 ethoxylation of 7 (AE7)
  • the granular laundry detergent composition of Table 2 is prepared by dry-mixing all of the above components (all except the AE7, Sokalan HP22 polymer and optical brightener, 7- (Diethylamino)-4-methyl-2H-chromen-2-one) in a continuous rotary mixer (drum diameter 0.6 meters, drum length 1.8 meters, 28 revolutions per min). The total mass flow rate of the powder feeds into the continuous rotary mixer set at 2913 kg/hr. A mixture of AE7 in liquid form and Sokalan HP22 polymer and 7-(Diethylamino)-4-methyl-2H-chromen-2-one in liquid form is sprayed on the particles as they pass through the continuous rotary mixer.
  • the mass flow rate of the liquid mixture is set to 88.9 kg/hr according to formulation in table 2.
  • the liquid mixture is atomized into droplets by air assisted nozzles operating at a air supply pressure of 5.2 bar gauge prior to liquid mixture addition into the continuous rotary mixer.
  • a granular detergent composition (Granular detergent A) is prepared where the liquid mixture is first emulsified (AE7 continuous phase) by passing through a high shear dynamic mixer (IKA Dispax-Reactor®; Model Size: DR2000/ Mixer Speed 4000 rpm) prior to atomizing and adding to powder.
  • a high shear dynamic mixer IKA Dispax-Reactor®; Model Size: DR2000/ Mixer Speed 4000 rpm

Abstract

L'invention concerne une composition comprenant un copolymère greffé amphiphile et un azurant optique, et un procédé de fabrication d'une composition de détergent granulaire comprenant les étapes consistant à : former une pâte de détergent aqueuse ; b) sécher par pulvérisation ladite pâte de détergent aqueuse pour former une pluralité de particules de détergent séchées par pulvérisation ; et c) former une émulsion comprenant un tensioactif, un copolymère greffé amphiphile, et un azurant optique ayant un ClogP compris entre 1 et 50; et d) ajouter l'émulsion obtenue à l'étape c) à au moins une portion de ladite pluralité de particules de détergent séchées par pulvérisation.
PCT/US2015/010614 2014-01-22 2015-01-08 Procédé de fabrication de compositions de détergent comprenant des polymères WO2015112342A1 (fr)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP3546554A1 (fr) * 2018-03-28 2019-10-02 The Procter & Gamble Company Procédé de séchage par atomisation

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Publication number Priority date Publication date Assignee Title
GB2551487A (en) * 2016-06-15 2017-12-27 Reckitt Benckiser Vanish Bv Composition

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Publication number Priority date Publication date Assignee Title
EP3546554A1 (fr) * 2018-03-28 2019-10-02 The Procter & Gamble Company Procédé de séchage par atomisation
WO2019190794A1 (fr) * 2018-03-28 2019-10-03 The Procter & Gamble Company Procédé de séchage par pulvérisation

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