WO2010133837A1 - Bleaching catalyst admixed with an insoluble support matrix - Google Patents

Bleaching catalyst admixed with an insoluble support matrix Download PDF

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Publication number
WO2010133837A1
WO2010133837A1 PCT/GB2010/001001 GB2010001001W WO2010133837A1 WO 2010133837 A1 WO2010133837 A1 WO 2010133837A1 GB 2010001001 W GB2010001001 W GB 2010001001W WO 2010133837 A1 WO2010133837 A1 WO 2010133837A1
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Prior art keywords
composition
composition according
bleach catalyst
bleach
accordance
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French (fr)
Inventor
Dora Zamuner
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Reckitt Benckiser UK Ltd
Reckitt Benckiser NV
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Reckitt Benckiser UK Ltd
Reckitt Benckiser NV
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    • 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
    • C11D3/39Organic or inorganic per-compounds
    • C11D3/3902Organic or inorganic per-compounds combined with specific additives
    • C11D3/3905Bleach activators or bleach catalysts
    • C11D3/3932Inorganic compounds or complexes
    • 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
    • C11D17/00Detergent materials or soaps characterised by their shape or physical properties
    • C11D17/04Detergent materials or soaps characterised by their shape or physical properties combined with or containing other objects
    • C11D17/041Compositions releasably affixed on a substrate or incorporated into a dispensing means

Definitions

  • the present invention relates to a composition
  • a composition comprising a bleaching catalyst admixed with a support matrix.
  • Inorganic peroxygen compounds especially hydrogen peroxide and solid peroxygen compounds which dissolve in water to release hydrogen peroxide, such as sodium perborate and sodium carbonate perhydrate, have long been used as oxidizing agents for purposes of disinfection and bleaching.
  • the oxidizing action of these substances in dilute solutions is heavily dependent on the temperature; for instance, with H 2 O 2 or perborate in alkaline bleaching liquors, sufficiently rapid bleaching of soiled textiles is obtained only at temperatures above about 8O 0 C.
  • bleach activators for which numerous proposals have been disclosed in the literature, principally from the classes of the N-acyl or 0-acyl compounds, examples being polyacylated alkylenediamines, especially tetraace- tylethylenediamine, acylated glycolurils, especially tetraacetylglycoluril, N-acylated hydantoins, hydrazides, triazoles, hydrotriazines, urazoles, diketopiperazines, sulfurylamides and cyanurates, and also carboxylic anhydrides, especially phthalic anhydride, carboxylic esters, especially sodium nonanoyloxybenzenesulfonate, sodium isononanoyloxybenzenesulfonate and acylated sugar derivatives, such as pentaacetylglucose .
  • bleach activators for which numerous proposals have been disclosed in the literature, principally from the classes of the N-acyl or 0-acyl compounds,
  • transition metal salts and transition metal complexes have been described, for example in European patent applications EP 392 592, EP 443 651, EP 458 397, EP 544 490, EP 549 271 and WO 01/48138, referred to as bleaching catalysts.
  • a composition comprising a bleaching catalyst admixed with an insoluble support matrix.
  • the matrix is insoluble in aqueous media.
  • the supported bleach catalyst of the present invention has a number of advantageous properties.
  • the principle advantageous property is that the bleach catalyst, particularly the transition metal thereof when present (when used in a washing / bleaching operation) is not substantive upon an item being washed or bleached. Thus detrimental damage to the item is drastically reduced.
  • Another advantage of the present invention is the catalysis of the oxidizing action and bleaching action of inorganic per- oxygen compound at low temperatures. Effective catalysis is observed below 8O 0 C and in particular from about 12°C to 40 0 C.
  • Another advantage of the present invention (when used in a washing / bleaching operation) is to allow for reduction of peroxygen amount and / or bleach activator (e.g. TAED) in a cleaning formulation while maintaining bleaching performance, thus allowing for cost reduction.
  • peroxygen amount and / or bleach activator e.g. TAED
  • a further advantage of the present invention is the repeated application of the novel solid oxidation bleaching catalyst. Such repeated applications can be useful in waste water treatment/water purification, for example in the textile industry and in pulp / cellulose bleaching operations.
  • the bleach catalyst comprises a transition metal compound based upon one or more of manganese, cop- per, iron, silver, platinum, cobalt, nickel, titanium, zirconium, tungsten, molybdenum, ruthenium, cerium, lanthanum or vanadium.
  • the bleach catalyst comprises a transition metal compound based upon manganese .
  • the manganese bleach catalyst may be selected from wide range of manganese compounds.
  • Suitable inorganic compounds (often salts) of manganese include hydrated / anhydrous halide (e.g. chloride / bromide), sulphate, sulphide, carbonate, nitrate, oxide.
  • suitable compounds (often salts) of manganese e.g.
  • Mn (II) include hydrated / anhydrous acetate, lactate, acetyl acetonate, cyclohexanebutyrate, phthalocya- nine, bis (ethylcyclopentadienyl) , bis (pentamethylcy- clopentadienyl) .
  • the bleach catalyst comprises manganese (II) acetate tetrahydrate and/or manganese (II) sulphate monohydrate .
  • the bleach catalyst may comprise :-
  • the bleach catalyst may comprise :-
  • the bleach catalyst may comprise :-
  • the bleach catalyst comprises from 0.001% to 10.00%, preferably from 0.01% to 5.00% more preferably from 0.15% to 2.5% of the composition, with the remainder of the composition comprising the support matrix.
  • the composition is for use in a washing operation, e.g. a textile washing operation in an automatic washing machine.
  • the composition may be used for multiple washing operations; in this case the composition may comprise a shaped article.
  • the shaped article is an article which is commonly used in a washing operation but which has been modified to comprise the composition of invention.
  • One particularly preferred such article is a "dosing ball", which are commonly used, particularly in laundry washing operations, for the dosing of the correct amount of detergent into the washing cycle.
  • dosing balls are by their nature reusable and thus the dosing ball is able to provide a bleach catalyst function over a plurality of wash cycles. The whole / a portion of the dosing may comprise the composition.
  • Another preferred article is a bucket / container which is used in combination with a bleach based formulation in a cleaning operation, e.g. for hard surface cleaning (floor cleaning or glass/window cleaning) or for a manual laundry operation.
  • the bucket / container are preferably made by injection moulding of plastic (PP, PE, ABS, PMMA, polyamide, PVC, PU or any other plastic material) .
  • a yet further article is a plastic table surface such as the kind used for manual laundry cleaning (in some developing countries) .
  • Another article is a brush used in combination with a bleach based formulation in a cleaning operation, e.g. for rubbing clothes/laundry, dish / house ware or for toilet / ceramic cleaning.
  • Further articles include roll balls for pre-treating laundry, cleaning cloths, internal plastic components of automatic laundry washing machines and dishwashing machine/, reusable plastic food containers / cutlery.
  • the shaped article may comprise a powder, a particle, a flake, a sheet or a fibre (e.g. a micro-fibre / nano-fibre) or a sponge.
  • a powder e.g. a powder, a particle, a flake, a sheet or a fibre (e.g. a micro-fibre / nano-fibre) or a sponge.
  • the shaped article may be in the form of a foam.
  • micro-structures may be agglomerated together into a macro-structure, e.g. the particles may be partially coalesced to make a honeycomb type structure or the fi- bres may be coalesced to make a woven / non-woven mat macro-structure .
  • the preferred particle size is in the range of from IOnm to 10mm, more preferably from 0.1mm to 10mm, most preferably from 0.3mm to 0.5mm.
  • the particles are preferably spherical.
  • the preferred diameter in the range of from 30 nm to 2000 ⁇ m, more preferably from 60nm to lOOO ⁇ m.
  • the support matrix generally comprises a polymeric material.
  • Suitable polymeric materials may be selected from the group of polyurethanes; polyolefins / hydrocarbons, e.g. polypropylene, polyethylene, polystyrene, polybuta- diene; polyamides; polyvinyl chloride; polyesters, e.g. poly methyl methacrylate, poly vinyl acetate; phenolic resins; copolymers, e.g. polymethylmethacrylate with n- butylacrylate and styrene; natural / modified natural polymers, e.g.
  • cellulose cellulose, rubber, latex, styrene- butadiene rubber, butyl rubber, chlorinated / hydrochlo- rinated rubber, nitrile rubber, vulcanized rubber, sili- conised rubber; polycarbonates; silicone resins (e.g. polydimethylsilicone) ; fluorinated resins, e.g. PTFE.
  • silicone resins e.g. polydimethylsilicone
  • fluorinated resins e.g. PTFE.
  • the support matrix may comprise an inorganic material.
  • suitable inorganic materials include zeolite, silica, alumina, zirconia, phosphates (e.g. AlPO 4 ), ceramic, glass, bauxite, anatase (TiC> 2 ) and carbon.
  • a method of producing a composition comprising a bleaching catalyst admixed with an insoluble support matrix.
  • the method comprises one or more techniques selected from the group of spinning, electro-spinning, solvent casting, thermal treatment, extrusion, co- extrusion, moulding, screw injection moulding, injection moulding, blow moulding, machine moulding, thermal press moulding, free moulding, compression moulding, transfer moulding, roto-moulding, jet moulding, steam chest moulding, sheet moulding, sheet moulding compound SMC, laminated moulding, cast moulding, moulding powder, moulding pressure, forming, vacuum forming, plug-assist vacuum forming, hot forming, free-blow forming, high-rate forming, magnetic forming, rubber forming, drape forming, plug-and-ring forming, hot powder forming, snapback forming, matched-die forming, cavity forming, cavity assist- forming, shock-forming, electrochemical forming, electro forming, pressing
  • thermal treatment involves heating the support material (e.g. a polymer such as PMMA) above its melting temperature and/or above its Tg (glass transition temperature) , admixing the bleach catalyst therewith and allowing the admixture to cool.
  • support material e.g. a polymer such as PMMA
  • Preferably casting involves dissolution of both the support and the oxidation catalyst in a solvent followed by deposition of the solution onto a surface (e.g. stainless steel or semiconductor material) and evaporation of the solvent with production of a free-standing solid support.
  • Suitable solvents include: chlorinated organic solvents (e.g. chloroform), ketones (e.g. acetone or methyl ethyl ketone) , dimethylsulfoxide (DMSO) , alcohols, aliphatic or aromatic hydrocarbons, glycol ethers or organic acids, (e.g. acetic acid or formic acid).
  • extrusion and co-extrusion involves passing a composition comprising the support and the catalyst through an extrusion machine or a press machine.
  • the extrusion is preferably performed at an elevated temperature which may be affected by heating or by the pressure applied by the extruder.
  • extrusion conditions depend to a degree upon the exact nature of the composition being extruded and by the type of machine used.
  • a suitable extrusion operating temperature is, for example, 90-260 0 C.
  • a suitable extrusion operating screw velocity is, for example, 25—250 rpm (rotation per minute) , preferably 50-125 rpm.
  • a suitable extrusion operating pressure is, for example, 30-250 bar.
  • the extrudate is preferably in the form of pellets or strands or noodles.
  • electro spinning involves dissolution of both the support and the oxidation catalyst in a solvent followed by discharge of the solvent admixture through an orifice into a chamber where evaporation of the solvent occurs.
  • Electric charging of the admixture occurs on or before discharge from the orifice. The charging of the admixture causes the admixture to distribute itself widely and sparsely leading to the production of fine fibres .
  • polymerisation involves formation of a polymeric support, by polymerisation of the polymer constituents in the presence of the oxidation catalyst to form a polymer matrix having the oxidation catalyst distributed there-through.
  • the polymer matrix may be porous and / or be in the form a sponge.
  • Preferred polymers suitable for use in this method include polymers formed in a condensation reaction such as polyesters and polyurethanes . Indeed polyurethanes are particularly suitable since foams and sponges may be readily made from such polymers.
  • the supported bleach catalyst is for incorporation in a detergent composition, e.g. a dishwashing, laundry, hard surface cleaning and / or disinfecting composition.
  • the composition is for use in the appropriate washing operation in a washing machine or other washing vessel such as a sink, bucket, etc.
  • the composition may be used in an additive (e.g. additives which are complementary to a detergent product used in a washing operation) or in addition to a product which contains a bleach.
  • the detergent composition may comprise a homogenous product, e.g. a uniform powder / liquid or alternatively the detergent composition may have a plurality of individual phases, e.g. such as a multi-phase tablet or a number of liquids contained in a multi-chamber container / bottle. Where a plurality of individual phases is present the supported bleach catalyst may be present in only a limited number of the phases, e.g. for a two phase tablet one phase may contain the supported bleach catalyst and one phase could be bleach catalyst free (and may contain a bleach, such as a source of peroxide / active oxygen) .
  • a homogenous product e.g. a uniform powder / liquid
  • the detergent composition may have a plurality of individual phases, e.g. such as a multi-phase tablet or a number of liquids contained in a multi-chamber container / bottle.
  • the supported bleach catalyst may be present in only a limited number of the phases, e.g. for a two phase tablet one phase may contain the
  • the detergent composition typically comprises at least one of surfactant (anionic, non-ionic, cationic or amphoteric) , builder, bleach, bleach activator, bleach stabilizer, bleaching catalyst, enzyme, polymer, co-builder, alkalizing agent, acidifying agent, anti-redeposition agent, silver protectant, colourant, optical brightener, UV stabilizer, fabric softener, fragrance, soil repellent, anticrease substance, antibacterial substance, colour protectant, discolouration inhibitor, vitamin, phyl- losilicate, odor-complexing substance, rinse aid, foam inhibitor, foaming agent, preservative, or auxiliary.
  • surfactant anionic, non-ionic, cationic or amphoteric
  • the cured resin formulation was in the form of a disc having a diameter of 5cm and a height of 1.3cm.
  • a solution containing sodium percarbonate and bleach TAED was compared vs. a solution containing PCB, TAED and the catalyst Mn (homogeneous) or vs. a solution containing PCB + TAED + the catalyst Mn (heterogeneous) .
  • UV/VIS Abs at 430nm to monitor the oxidation rate on substrate (saffron).

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  • 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)
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  • Inorganic Chemistry (AREA)
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  • Catalysts (AREA)

Abstract

A composition comprises a bleaching catalyst admixed with an insoluble support matrix.

Description

BLEACHING CATALYST ADMIXED WITH AN INSOLUBLE
SUPPORT MATRIX
The present invention relates to a composition comprising a bleaching catalyst admixed with a support matrix.
Inorganic peroxygen compounds, especially hydrogen peroxide and solid peroxygen compounds which dissolve in water to release hydrogen peroxide, such as sodium perborate and sodium carbonate perhydrate, have long been used as oxidizing agents for purposes of disinfection and bleaching. The oxidizing action of these substances in dilute solutions is heavily dependent on the temperature; for instance, with H2O2 or perborate in alkaline bleaching liquors, sufficiently rapid bleaching of soiled textiles is obtained only at temperatures above about 8O0C. At lower temperatures the oxidizing action of the inorganic peroxygen compounds can be enhanced by adding what are called bleach activators, for which numerous proposals have been disclosed in the literature, principally from the classes of the N-acyl or 0-acyl compounds, examples being polyacylated alkylenediamines, especially tetraace- tylethylenediamine, acylated glycolurils, especially tetraacetylglycoluril, N-acylated hydantoins, hydrazides, triazoles, hydrotriazines, urazoles, diketopiperazines, sulfurylamides and cyanurates, and also carboxylic anhydrides, especially phthalic anhydride, carboxylic esters, especially sodium nonanoyloxybenzenesulfonate, sodium isononanoyloxybenzenesulfonate and acylated sugar derivatives, such as pentaacetylglucose . By addition of these substances the bleaching action of aqueous peroxide liquors can be increased to such an extent that even at temperatures around 6O0C essentially the same activities occur as with the peroxide liquor alone at 95°C. Given the concern for energy-saving laundering and bleaching methods, in recent years application temperatures well below 600C have gained in importance, in particular below 45°C down to the cold water temperature, below 200C.
Previously the use of transition metal salts and transition metal complexes has been described, for example in European patent applications EP 392 592, EP 443 651, EP 458 397, EP 544 490, EP 549 271 and WO 01/48138, referred to as bleaching catalysts.
It has now been observed that textiles, particularly coloured textiles, fade after a number of washes in the presence of a bleach catalyst. It is theorised that some catalysts previously used not only catalyze the activity of the peroxygen compound but also remain at least partly on their surfaces being bleached, and even when the cleaning operation has ended. These transition metal salts can then be oxidized and so cause colour damage, and, in extreme cases, the risk of oxidative damage to the textiles since they directly contact the textile. As an example a deposit of Mn (II), is readily oxidized to Mn (IV) dioxide, which is a very strong oxidizing agent, particularly toward easily oxidizable substances, such as organic dye compounds.
All of the bleaching catalysts known have the disadvantage that they are brought into intimate contact with the surfaces of the articles being treated and as such typically a portion of the catalyst adheres to those surfaces or even penetrate those surfaces. This gives rise to a risk of unwanted colour changes and in rare cases, there may even be holes / tears, as a result of fibre damage. According to a first aspect of the invention there is provided a composition comprising a bleaching catalyst admixed with an insoluble support matrix.
Preferably the matrix is insoluble in aqueous media.
It has been found that the supported bleach catalyst of the present invention has a number of advantageous properties. The principle advantageous property is that the bleach catalyst, particularly the transition metal thereof when present (when used in a washing / bleaching operation) is not substantive upon an item being washed or bleached. Thus detrimental damage to the item is drastically reduced.
Another advantage of the present invention (when used in a washing / bleaching operation) is the catalysis of the oxidizing action and bleaching action of inorganic per- oxygen compound at low temperatures. Effective catalysis is observed below 8O0C and in particular from about 12°C to 400C.
Another advantage of the present invention (when used in a washing / bleaching operation) is to allow for reduction of peroxygen amount and / or bleach activator (e.g. TAED) in a cleaning formulation while maintaining bleaching performance, thus allowing for cost reduction.
Being reusable and recoverable, a further advantage of the present invention is the repeated application of the novel solid oxidation bleaching catalyst. Such repeated applications can be useful in waste water treatment/water purification, for example in the textile industry and in pulp / cellulose bleaching operations.
Preferably the bleach catalyst comprises a transition metal compound based upon one or more of manganese, cop- per, iron, silver, platinum, cobalt, nickel, titanium, zirconium, tungsten, molybdenum, ruthenium, cerium, lanthanum or vanadium. Most preferably the bleach catalyst comprises a transition metal compound based upon manganese .
The manganese bleach catalyst may be selected from wide range of manganese compounds. Suitable inorganic compounds (often salts) of manganese (e.g. Mn (II)) include hydrated / anhydrous halide (e.g. chloride / bromide), sulphate, sulphide, carbonate, nitrate, oxide. Further examples of suitable compounds (often salts) of manganese (e.g. Mn (II)) include hydrated / anhydrous acetate, lactate, acetyl acetonate, cyclohexanebutyrate, phthalocya- nine, bis (ethylcyclopentadienyl) , bis (pentamethylcy- clopentadienyl) .
Most preferably the bleach catalyst comprises manganese (II) acetate tetrahydrate and/or manganese (II) sulphate monohydrate .
Alternatively the bleach catalyst may comprise :-
Figure imgf000005_0001
( 1 , 8 - diethyl-1 , 4 , 8 , 11-TetraAzaCycloTetraDecane ) manganese ( I I ) chloride [Mn-TACTD] . Alternatively the bleach catalyst may comprise :-
Mangan organic
Figure imgf000006_0001
Alternatively the bleach catalyst may comprise :-
Figure imgf000006_0002
Generally the bleach catalyst comprises from 0.001% to 10.00%, preferably from 0.01% to 5.00% more preferably from 0.15% to 2.5% of the composition, with the remainder of the composition comprising the support matrix.
Generally the composition is for use in a washing operation, e.g. a textile washing operation in an automatic washing machine. The composition may be used for multiple washing operations; in this case the composition may comprise a shaped article.
Preferably the shaped article is an article which is commonly used in a washing operation but which has been modified to comprise the composition of invention. One particularly preferred such article is a "dosing ball", which are commonly used, particularly in laundry washing operations, for the dosing of the correct amount of detergent into the washing cycle. Such dosing balls are by their nature reusable and thus the dosing ball is able to provide a bleach catalyst function over a plurality of wash cycles. The whole / a portion of the dosing may comprise the composition.
Another preferred article is a bucket / container which is used in combination with a bleach based formulation in a cleaning operation, e.g. for hard surface cleaning (floor cleaning or glass/window cleaning) or for a manual laundry operation. The bucket / container are preferably made by injection moulding of plastic (PP, PE, ABS, PMMA, polyamide, PVC, PU or any other plastic material) .
A yet further article is a plastic table surface such as the kind used for manual laundry cleaning (in some developing countries) .
Another article is a brush used in combination with a bleach based formulation in a cleaning operation, e.g. for rubbing clothes/laundry, dish / house ware or for toilet / ceramic cleaning.
Further articles include roll balls for pre-treating laundry, cleaning cloths, internal plastic components of automatic laundry washing machines and dishwashing machine/, reusable plastic food containers / cutlery.
Alternatively the shaped article may comprise a powder, a particle, a flake, a sheet or a fibre (e.g. a micro-fibre / nano-fibre) or a sponge.
The shaped article may be in the form of a foam.
These micro-structures may be agglomerated together into a macro-structure, e.g. the particles may be partially coalesced to make a honeycomb type structure or the fi- bres may be coalesced to make a woven / non-woven mat macro-structure .
Where the support is a particle, the preferred particle size is in the range of from IOnm to 10mm, more preferably from 0.1mm to 10mm, most preferably from 0.3mm to 0.5mm. The particles are preferably spherical.
Where the support is fibre, the preferred diameter in the range of from 30 nm to 2000μm, more preferably from 60nm to lOOOμm.
The support matrix generally comprises a polymeric material. Suitable polymeric materials may be selected from the group of polyurethanes; polyolefins / hydrocarbons, e.g. polypropylene, polyethylene, polystyrene, polybuta- diene; polyamides; polyvinyl chloride; polyesters, e.g. poly methyl methacrylate, poly vinyl acetate; phenolic resins; copolymers, e.g. polymethylmethacrylate with n- butylacrylate and styrene; natural / modified natural polymers, e.g. cellulose, rubber, latex, styrene- butadiene rubber, butyl rubber, chlorinated / hydrochlo- rinated rubber, nitrile rubber, vulcanized rubber, sili- conised rubber; polycarbonates; silicone resins (e.g. polydimethylsilicone) ; fluorinated resins, e.g. PTFE.
The support matrix may comprise an inorganic material. Suitable inorganic materials include zeolite, silica, alumina, zirconia, phosphates (e.g. AlPO4), ceramic, glass, bauxite, anatase (TiC>2) and carbon.
According to a second aspect of the invention there is provided a method of producing a composition comprising a bleaching catalyst admixed with an insoluble support matrix. Preferably the method comprises one or more techniques selected from the group of spinning, electro-spinning, solvent casting, thermal treatment, extrusion, co- extrusion, moulding, screw injection moulding, injection moulding, blow moulding, machine moulding, thermal press moulding, free moulding, compression moulding, transfer moulding, roto-moulding, jet moulding, steam chest moulding, sheet moulding, sheet moulding compound SMC, laminated moulding, cast moulding, moulding powder, moulding pressure, forming, vacuum forming, plug-assist vacuum forming, hot forming, free-blow forming, high-rate forming, magnetic forming, rubber forming, drape forming, plug-and-ring forming, hot powder forming, snapback forming, matched-die forming, cavity forming, cavity assist- forming, shock-forming, electrochemical forming, electro forming, pressing, cold forging and/or polymerisation.
Preferably thermal treatment (or thermoforming) involves heating the support material (e.g. a polymer such as PMMA) above its melting temperature and/or above its Tg (glass transition temperature) , admixing the bleach catalyst therewith and allowing the admixture to cool.
Preferably casting involves dissolution of both the support and the oxidation catalyst in a solvent followed by deposition of the solution onto a surface (e.g. stainless steel or semiconductor material) and evaporation of the solvent with production of a free-standing solid support. Suitable solvents include: chlorinated organic solvents (e.g. chloroform), ketones (e.g. acetone or methyl ethyl ketone) , dimethylsulfoxide (DMSO) , alcohols, aliphatic or aromatic hydrocarbons, glycol ethers or organic acids, (e.g. acetic acid or formic acid).
Preferably extrusion and co-extrusion involves passing a composition comprising the support and the catalyst through an extrusion machine or a press machine. The extrusion is preferably performed at an elevated temperature which may be affected by heating or by the pressure applied by the extruder.
The extrusion conditions depend to a degree upon the exact nature of the composition being extruded and by the type of machine used. A suitable extrusion operating temperature is, for example, 90-2600C. A suitable extrusion operating screw velocity is, for example, 25—250 rpm (rotation per minute) , preferably 50-125 rpm. A suitable extrusion operating pressure is, for example, 30-250 bar. The extrudate is preferably in the form of pellets or strands or noodles.
Preferably electro spinning involves dissolution of both the support and the oxidation catalyst in a solvent followed by discharge of the solvent admixture through an orifice into a chamber where evaporation of the solvent occurs. Electric charging of the admixture occurs on or before discharge from the orifice. The charging of the admixture causes the admixture to distribute itself widely and sparsely leading to the production of fine fibres .
Preferably polymerisation involves formation of a polymeric support, by polymerisation of the polymer constituents in the presence of the oxidation catalyst to form a polymer matrix having the oxidation catalyst distributed there-through. The polymer matrix may be porous and / or be in the form a sponge. Preferred polymers suitable for use in this method include polymers formed in a condensation reaction such as polyesters and polyurethanes . Indeed polyurethanes are particularly suitable since foams and sponges may be readily made from such polymers. Preferably the supported bleach catalyst is for incorporation in a detergent composition, e.g. a dishwashing, laundry, hard surface cleaning and / or disinfecting composition. Generally the composition is for use in the appropriate washing operation in a washing machine or other washing vessel such as a sink, bucket, etc. Alternatively the composition may be used in an additive (e.g. additives which are complementary to a detergent product used in a washing operation) or in addition to a product which contains a bleach.
The detergent composition may comprise a homogenous product, e.g. a uniform powder / liquid or alternatively the detergent composition may have a plurality of individual phases, e.g. such as a multi-phase tablet or a number of liquids contained in a multi-chamber container / bottle. Where a plurality of individual phases is present the supported bleach catalyst may be present in only a limited number of the phases, e.g. for a two phase tablet one phase may contain the supported bleach catalyst and one phase could be bleach catalyst free (and may contain a bleach, such as a source of peroxide / active oxygen) .
The detergent composition typically comprises at least one of surfactant (anionic, non-ionic, cationic or amphoteric) , builder, bleach, bleach activator, bleach stabilizer, bleaching catalyst, enzyme, polymer, co-builder, alkalizing agent, acidifying agent, anti-redeposition agent, silver protectant, colourant, optical brightener, UV stabilizer, fabric softener, fragrance, soil repellent, anticrease substance, antibacterial substance, colour protectant, discolouration inhibitor, vitamin, phyl- losilicate, odor-complexing substance, rinse aid, foam inhibitor, foaming agent, preservative, or auxiliary. The invention is now illustrated by reference to the following non-limiting examples.
Examples
Example 1 : Catalyst Preparation
2Og of Polydimethylsilicone (PDMS) (Sylgard 184 by Dow
Corning) was weighed in a beaker. lOmg of catalyst Mn-
TACN or Mn Acetate and Ig of curing agent was added and mixed. The admixture was left for 24 hours to cure. The cured resin formulation was in the form of a disc having a diameter of 5cm and a height of 1.3cm.
Example 2 : Oxidation Catalysis Study
The following reagents were prepared, in deionised water.
Figure imgf000012_0001
A solution containing sodium percarbonate and bleach TAED was compared vs. a solution containing PCB, TAED and the catalyst Mn (homogeneous) or vs. a solution containing PCB + TAED + the catalyst Mn (heterogeneous) . Protocol Used: Beaker Test
Saffron solution (fresh, protected from light)
Deionised water
Temperature: 200C
Reaction studied over 30 minutes.
UV/VIS Abs at 430nm to monitor the oxidation rate on substrate (saffron).
Note: the lower the absorbance residue, the better the catalytic effect/performance.
Results
Figure imgf000013_0001
(Each value is the average of three measurements.
The results show that the use of Mn-TACN is effective as oxidation catalyst (vs. no catalyst) and that heterogeneous catalysis is good on the bleaching of saffron.

Claims

1. A composition comprising a catalyst admixed with an insoluble support matrix.
2. A composition comprising a bleaching catalyst admixed with an insoluble support matrix.
3. A composition according to claim 2, wherein the bleach catalyst comprises a transition metal compound based upon one or more of manganese, copper, iron, silver, platinum, cobalt, nickel, titanium, vanadium, cerium, lanthanum, zirconium, tungsten, molybdenum, ruthenium.
4. A composition according to claim 3, wherein the bleach catalyst comprises a transition metal compound based upon manganese .
5. A composition according to claim 4, wherein the bleach catalyst comprises a hydrated / anhydrous compound of manganese selected from the group comprising the halide
(chloride/bromide) , sulphate, sulphide, carbonate, nitrate, oxide, acetate, lactate, acetyl acetonate, cyclo- hexanebutyrate, phthalocyanine, gluconate, bis (ethylcy- clopentadienyl) , bis (pentamethylcyclopentadienyl) , polyol, sorbitol, iditol, mannitol, xylithol, arabintol, lactose, dulsitol, adonitol, erythritol, inositol, cathe- col .
6. A composition according to claim 4, wherein the bleach catalyst comprises:-
Figure imgf000015_0001
(1, 8 - diethyl-1 , 4, 8, 11 - TetraAzaCycloTetraDecane) Manganese (II) chloride.
7. A composition according to claim 4, wherein the bleach catalyst comprises :-
Mangan organic
Figure imgf000015_0002
8. A composition according to claim 3, wherein the bleach catalyst comprises: manganese (II) acetate tetrahydrate and/or manganese (II) sulphate monohydrate.
9. A composition according to any one of the preceding claims, wherein the bleach catalyst comprises from 0.0001% to 20%, preferably from 0.001% to 10.00%, preferably from 0.01% to 5.00% more preferably from 0.15% to 2.5% of the composition.
10. A composition according to any one of the preceding claims where the matrix exhibits porosity.
11. A composition according to any one of the preceding claims, wherein the support matrix is a shaped article or gadget.
12. A composition according to claim 11, wherein the shaped article is a detergent dosing ball or a part of an automatic washing machine.
13. A composition according to claim 11, wherein the support is at least one of a powder, a particle, a flake, an agglomerate, a sponge, a sheet or a fibre (e.g. a micro- fibre or a nano-fibre) .
14. A composition according to claim 13, wherein the support is a particle having a particle diameter in the range of from IOnm to 10mm.
15. A composition according to claim 13, wherein the support is a fibre having a diameter in the range of from 30 nm to 2000μm, more preferably from 60nm to lOOOμm.
16. A composition in accordance with any one of preceding claims in which the support matrix comprises a polymeric material selected from the group of poly methyl methacry- late, polyurethanes; polyolefins / hydrocarbons, e.g. polypropylene, polyethylene, polystyrene, polybutadiene; polyamides; polyvinyl chloride; polyesters, poly vinyl acetate; phenolic resins; copolymers, e.g. polymethylmethacrylate with n-butylacrylate and styrene; natural / modified natural polymers, e.g. cellulose, rubber, latex, styrene-butadiene rubber, butyl rubber, chlorinated / hy- drochlorinated rubber, nitrile rubber, vulcanized rubber, siliconised rubber; polycarbonates; silicone resins (e.g. polydimethylsilicone) ; fluorinated resins, e.g. PTFE.
17. A composition in accordance with any one of claims 1 to 15 in which the support matrix comprises one or more of zeolite silica, alumina, zirconia, phosphates (e.g. AlPO4) , ceramic, glass, bauxite, anatase (TiO2), carbon.
18. A method of producing the bleach catalyst composition in accordance with any one of preceding claims in which the technique of thermal treatment, casting, extrusion and / or electro-spinning is used.
19. A method of producing the bleach catalyst composition in accordance with any one of preceding claims in which the technique of driving a thermoplastic polymer above its glass transition temperature is used.
20. A method of producing the bleach catalyst composition in accordance with claim 18, in which the technique of casting / solvent casting is used.
21. A method of producing the bleach catalyst composition in accordance with claim 19, in which the technique of extrusion is used.
22. A method of producing the bleach catalyst composition in accordance with claim 18, in which the technique of electro-spinning is used.
23. A detergent composition comprising a bleach catalyst composition in accordance with any one of claims 1 to 17.
24. A detergent comprising the composition any one of claims 1 to 17 and at least one of surfactant (non-ionic, anionic, cationic or amphoteric) , builder, bleach, bleach activator, bleach stabilizer, bleaching catalyst, enzyme, polymer, cobuilder, alkalizing agent, acidifying agent, antiredeposition agent, silver protectant, colourant, optical brightener, UV stabilizer, fabric softener, fragrance, soil repellent, anticrease substance, antibacterial substance, colour protectant, discolouration inhibitor, vitamin, phyllosilicate, odor-complexing substance, rinse aid, foam inhibitor, foaming agent, preservative, or auxiliary.
25. Use of a detergent composition according to claim 24 in a dishwashing, laundry and / or hard surface cleaning operation and/ or a sanitizer/disinfectant operation.
26. Use of a heterogeneous catalyst according to claim 1 for application in waste water treatment, in the textile industry, in hair care / hair bleaching formulations, in pulp and cellulose bleaching operations.
PCT/GB2010/001001 2009-05-20 2010-05-19 Bleaching catalyst admixed with an insoluble support matrix Ceased WO2010133837A1 (en)

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