EP0336635A1 - Process for preparing a coloured granular alkali metal silicate - Google Patents
Process for preparing a coloured granular alkali metal silicate Download PDFInfo
- Publication number
- EP0336635A1 EP0336635A1 EP19890303091 EP89303091A EP0336635A1 EP 0336635 A1 EP0336635 A1 EP 0336635A1 EP 19890303091 EP19890303091 EP 19890303091 EP 89303091 A EP89303091 A EP 89303091A EP 0336635 A1 EP0336635 A1 EP 0336635A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- granules
- coloured
- alkali metal
- silicate
- granular material
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- 229910052910 alkali metal silicate Inorganic materials 0.000 title claims abstract description 23
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 4
- 239000008187 granular material Substances 0.000 claims abstract description 48
- 239000003599 detergent Substances 0.000 claims abstract description 36
- BPQQTUXANYXVAA-UHFFFAOYSA-N Orthosilicate Chemical compound [O-][Si]([O-])([O-])[O-] BPQQTUXANYXVAA-UHFFFAOYSA-N 0.000 claims abstract description 11
- 239000000463 material Substances 0.000 claims abstract description 9
- 239000004115 Sodium Silicate Substances 0.000 claims abstract description 8
- 229910052911 sodium silicate Inorganic materials 0.000 claims abstract description 8
- NTHWMYGWWRZVTN-UHFFFAOYSA-N sodium silicate Chemical compound [Na+].[Na+].[O-][Si]([O-])=O NTHWMYGWWRZVTN-UHFFFAOYSA-N 0.000 claims abstract description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 6
- 239000000203 mixture Substances 0.000 claims description 19
- 239000000843 powder Substances 0.000 claims description 12
- 239000000049 pigment Substances 0.000 claims description 8
- 238000005507 spraying Methods 0.000 claims description 6
- 238000001035 drying Methods 0.000 claims description 5
- RBTKNAXYKSUFRK-UHFFFAOYSA-N heliogen blue Chemical compound [Cu].[N-]1C2=C(C=CC=C3)C3=C1N=C([N-]1)C3=CC=CC=C3C1=NC([N-]1)=C(C=CC=C3)C3=C1N=C([N-]1)C3=CC=CC=C3C1=N2 RBTKNAXYKSUFRK-UHFFFAOYSA-N 0.000 claims description 4
- 238000001816 cooling Methods 0.000 claims description 3
- 239000000725 suspension Substances 0.000 claims description 2
- 239000013078 crystal Substances 0.000 claims 1
- 238000000034 method Methods 0.000 abstract description 12
- 239000000243 solution Substances 0.000 description 12
- 239000000975 dye Substances 0.000 description 10
- 239000002245 particle Substances 0.000 description 7
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 6
- 239000002585 base Substances 0.000 description 6
- 150000004760 silicates Chemical class 0.000 description 5
- 229910019142 PO4 Inorganic materials 0.000 description 4
- 238000009826 distribution Methods 0.000 description 4
- -1 phosphates Chemical class 0.000 description 4
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- KKCBUQHMOMHUOY-UHFFFAOYSA-N Na2O Inorganic materials [O-2].[Na+].[Na+] KKCBUQHMOMHUOY-UHFFFAOYSA-N 0.000 description 3
- PMZURENOXWZQFD-UHFFFAOYSA-L Sodium Sulfate Chemical compound [Na+].[Na+].[O-]S([O-])(=O)=O PMZURENOXWZQFD-UHFFFAOYSA-L 0.000 description 3
- PMYUVOOOQDGQNW-UHFFFAOYSA-N hexasodium;trioxido(trioxidosilyloxy)silane Chemical compound [Na+].[Na+].[Na+].[Na+].[Na+].[Na+].[O-][Si]([O-])([O-])O[Si]([O-])([O-])[O-] PMYUVOOOQDGQNW-UHFFFAOYSA-N 0.000 description 3
- 239000010452 phosphate Substances 0.000 description 3
- 235000021317 phosphate Nutrition 0.000 description 3
- 239000000377 silicon dioxide Substances 0.000 description 3
- 238000005406 washing Methods 0.000 description 3
- KEZYHIPQRGTUDU-UHFFFAOYSA-N 2-[dithiocarboxy(methyl)amino]acetic acid Chemical compound SC(=S)N(C)CC(O)=O KEZYHIPQRGTUDU-UHFFFAOYSA-N 0.000 description 2
- 229910021536 Zeolite Inorganic materials 0.000 description 2
- 238000007664 blowing Methods 0.000 description 2
- 239000011248 coating agent Substances 0.000 description 2
- 238000000576 coating method Methods 0.000 description 2
- 229910052681 coesite Inorganic materials 0.000 description 2
- 229910052906 cristobalite Inorganic materials 0.000 description 2
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 239000004615 ingredient Substances 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- NBIIXXVUZAFLBC-UHFFFAOYSA-K phosphate Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 description 2
- 230000000717 retained effect Effects 0.000 description 2
- 150000003839 salts Chemical class 0.000 description 2
- 235000012239 silicon dioxide Nutrition 0.000 description 2
- 229910052938 sodium sulfate Inorganic materials 0.000 description 2
- 235000011152 sodium sulphate Nutrition 0.000 description 2
- 239000002904 solvent Substances 0.000 description 2
- 239000007921 spray Substances 0.000 description 2
- 229910052682 stishovite Inorganic materials 0.000 description 2
- 229910052905 tridymite Inorganic materials 0.000 description 2
- 239000010457 zeolite Substances 0.000 description 2
- 239000007864 aqueous solution Substances 0.000 description 1
- 239000007900 aqueous suspension Substances 0.000 description 1
- 239000011230 binding agent Substances 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 238000005056 compaction Methods 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000002425 crystallisation Methods 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- 238000010790 dilution Methods 0.000 description 1
- 239000012895 dilution Substances 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 238000010981 drying operation Methods 0.000 description 1
- 238000010410 dusting Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000009472 formulation Methods 0.000 description 1
- 239000013538 functional additive Substances 0.000 description 1
- 238000005469 granulation Methods 0.000 description 1
- 230000003179 granulation Effects 0.000 description 1
- 150000004687 hexahydrates Chemical class 0.000 description 1
- 239000003112 inhibitor Substances 0.000 description 1
- 229910010272 inorganic material Inorganic materials 0.000 description 1
- 239000011147 inorganic material Substances 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- HWGNBUXHKFFFIH-UHFFFAOYSA-I pentasodium;[oxido(phosphonatooxy)phosphoryl] phosphate Chemical compound [Na+].[Na+].[Na+].[Na+].[Na+].[O-]P([O-])(=O)OP([O-])(=O)OP([O-])([O-])=O HWGNBUXHKFFFIH-UHFFFAOYSA-I 0.000 description 1
- 150000003013 phosphoric acid derivatives Chemical class 0.000 description 1
- 238000005204 segregation Methods 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 235000019795 sodium metasilicate Nutrition 0.000 description 1
- 239000001488 sodium phosphate Substances 0.000 description 1
- 229910000162 sodium phosphate Inorganic materials 0.000 description 1
- 235000019832 sodium triphosphate Nutrition 0.000 description 1
- 238000007711 solidification Methods 0.000 description 1
- 230000008023 solidification Effects 0.000 description 1
- 238000001694 spray drying Methods 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- RYFMWSXOAZQYPI-UHFFFAOYSA-K trisodium phosphate Chemical compound [Na+].[Na+].[Na+].[O-]P([O-])([O-])=O RYFMWSXOAZQYPI-UHFFFAOYSA-K 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11D—DETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
- C11D3/00—Other compounding ingredients of detergent compositions covered in group C11D1/00
- C11D3/02—Inorganic compounds ; Elemental compounds
- C11D3/04—Water-soluble compounds
- C11D3/08—Silicates
-
- 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
- C11D17/00—Detergent materials or soaps characterised by their shape or physical properties
- C11D17/0039—Coated compositions or coated components in the compositions, (micro)capsules
-
- 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
Definitions
- the invention relates to coloured granules which can be used as speckles in detergent powders and to a process for manufacturing speckles.
- Coloured granules in detergent compositions are well-known in the art, especially in phosphate containing detergent compositions and the detergent speckles therefore are usually mainly based on soluble inorganic salts like phosphates, especially sodium triphosphate, sodium sulphate or mixtures therefrom, which granules have been coated/impregnated with a solution or dispersion of a colourant i.e. a dye or pigment.
- a colourant i.e. a dye or pigment.
- the speckles are green or blue. Speckles give the detergent composition a more attractive consumer appeal, moreover it is possible to incorporate special purpose ingredients via the speckles in the detergent composition.
- the amount of colourant in the granular material is so low as not to interfere with the washing process, moreover the speckles should be bright coloured and if possible the detergent speckle base material should serve a useful and practical purpose in the detergent composition.
- the detergent speckle base material should serve a useful and practical purpose in the detergent composition.
- the present invention provides coloured detergent speckles satisfying most of the above requirements in the form of granular alkali metal silicate which has been coated with a colourant i.e. a pigment or dye.
- the alkali metal silicate is sodium silicate, more preferably metasilicate and/or disilicate.
- Silicates have the functions of improving the washing effect and of corrosion inhibitor in detergent composition and consequently are a functional additive.
- silicate hydrates as the base material for the speckles according to the present invention and sodium silicate penta- and/or hexahydrate give optimal results.
- sodium silicate penta- and/or hexahydrate give optimal results.
- the base material for the speckles consists substantially of sodium silicate it is, however, also possible to use as the base material for the speckles a mixture of materials in which at least 50% of the dry weight consists ot alkali metal silicate, the remainder being other inorganic materials like eg. zeolite, sodium sulfate or sodium phosphate if the latter can be tolerated in the eventual detergent composition.
- the coloured silicate granules according to the present invention usually have an average particle size of 0.2 - 2mm, preferably from 0.8 to 1.6 mm, diameter. Granules with an spherical shape have advantages and then the diameter is taken to determine the size. Of course the actual size of the speckles desired depends on that of the detergent powder in which the speckles are incorporated.
- the colourant i.e. dye or pigment, which forms a coating on the alkali metal silicate granules is normally present in an amount of 0.1 to 2.0% (w.w.) of the granules.
- the colourant usually is a commercially available dye and compounds like Monastral Blue and Monastral Green + Unidispers Blue (ex CIBA-Geigy) are preferred. (Monastral dyes are ex ICI, England.)
- the coloured detergent speckles are usually incorporated in detergent powders in a level between 0.1 - 5%, preferably between 0.2 and 2.0%, by weight of the total detergent composition.
- the invention extends particularly to the use of sodium silicate having Na2O:SiO2 ratios from 1:1.2 to 1:3.3, preferably 1:1.5 to 1:3.0.
- the higher ratios are generally less preferred because of slower solution.
- the granules of alkali metal silicate can be prepared by a number of suitable procedures, for example metasilicate (Na2O:Silica ratio 1:1) can be granulated in a rotary barrel as described in GB 1149859 (Baker-Holloway).
- silicates in compacted form is particularly valuable for speckles intended for the higher density detergent powder compositions, that is having a bulk density above 700 g/l, preferably above 800 g/l.
- Sodium disilicate can be prepared with a bulk density between 700 and 900 g/l by compaction between rollers.
- Sodium metasilicate can be prepared with a bulk density between 880 and 1,000 g/l using granulation in a rotary barrel.
- a binder eg. silicate solution
- detergent speckles are manufactured by a number of methods.
- One method involved the spray-drying of a special coloured slurry but the obvious disadvantage is that thorough cleaning is required before normal detergent powder can be produced again.
- Another method involved spraying a coloured solution onto a spray-dried detergent powder, but this requires, as the previous method, a large amount of coloured solution.
- a solution of a colourant that also comprises a hydratable salt, preferably a warm and concentrated solution, to facilitate subsequent crystallisation.
- zeolite containing detergent compositions this method was found not quite practical because a high percentage of colourant was required.
- the coloured detergent speckles according to the present invention which are based on alkali metal silicate, can be prepared by spraying under suitable conditions a solution of a colourant on granular alkali metal silicate, which is kept in constant motion so as to avoid caking. This can be done e.g. by carrying out the operation in a fluidized bed, or in a mixer, followed by drying while keeping the granules in constant motion.
- Suitable equipment for this technique comprises fluidized beds, nozzles for the coloured liquid, for hot and cool air, Tellschig*-type mixers consisting of rotating drums and fitted with a spray-nozzle, Loedige-type mixers consisting of fixed drums with an internal scraper fitted with a spray-nozzle, Nauta*-mixers of a type consisting of a conical vessel with a rotating scraper fitted with a spray-nozzle etc. (*stands for tradename).
- the amount of dye solution or pigment suspension sprayed on the alkali metal silicate granules normally lies between 0.1 and 5.0% by weight, preferably between 0.5 - 2.0%, calculated on the alkali metal silicate.
- the particle size distribution of the starting granules determines the size of the coloured speckles and most alkali metal silicate granules are available in various, often uniform or narrow particle size ranges which can be chosen dependent on the size desired in the detergent composition.
- the solution which is sprayed onto the granular alkali metal silicate materiai usually contains from 0.05 to 50% of colourant preferably completely dissolved.
- solubility of e.g. the dye in the solvent to be observed. Water is preferred as the solvent but it is sometimes advantageous to use (aqueous) methanol to increase the solubility of the dye.
- the quantity of liquid sprayed onto the granules is normally between 0.1 and 5%, preferably between 0.5 and 2%, by weight calculated on the silicate and spraying normally is completed within a few minutes to half an hour, 2 to 10 minutes is typical.
- the detergent speckles so obtained are distinctive, of uniform colour, resistant to attrition and have virtually the same particle size distribution as the alkali metal silicate starting granules have.
- alkali metal silicates as a core for speckles is particularly efficient because, for one or more of the reasons,
- 1.5 kg sodium metasilicate pentahydrate granules with a particle size between 0.2 and 1.2 mm was placed in a Loedige mixer of 5 litres. The mixer was switched on and the contents were pre-heated to 35 - 45°C by blowing in hot air with a temperature of 50°C. An aqueous solution containing 25% by weight of Monastral Blue was sprayed onto the granules for 5 minutes. The amount of solution sprayed onto the granules was 1% by weight calculated on the metasilicate. Consequently only 0.25% of dye was used relative to the metasilicate. Drying was also carried out at a temperature of 35-45°C for a period of 20 minutes.
- the water content of the metasilicate was monitored during the drying and kept at around 43% by weight.
- the detergent speckles were then cooled to 20°C by blowing in cool air.
- the detergent speckles thus obtained showed excellent brightness, a deep hue, were uniformly coloured, colour-stable and the original particle size distribution had substantially been retained. Whe mixed in a detergent powder at a level of 1% by weight they imparted an excellent consumer appeal to the product.
- Sodium disilicate Na2O:SiO2 ratio of 1:2 was spray dried to provide granules.
Landscapes
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Wood Science & Technology (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Detergent Compositions (AREA)
- Silicates, Zeolites, And Molecular Sieves (AREA)
Abstract
Description
- The invention relates to coloured granules which can be used as speckles in detergent powders and to a process for manufacturing speckles.
- Coloured granules in detergent compositions (detergent speckles) are well-known in the art, especially in phosphate containing detergent compositions and the detergent speckles therefore are usually mainly based on soluble inorganic salts like phosphates, especially sodium triphosphate, sodium sulphate or mixtures therefrom, which granules have been coated/impregnated with a solution or dispersion of a colourant i.e. a dye or pigment. Preferable the speckles are green or blue. Speckles give the detergent composition a more attractive consumer appeal, moreover it is possible to incorporate special purpose ingredients via the speckles in the detergent composition.
- It is desirable that the amount of colourant in the granular material is so low as not to interfere with the washing process, moreover the speckles should be bright coloured and if possible the detergent speckle base material should serve a useful and practical purpose in the detergent composition. For "zero-phosphate detergent compositions" of course no phosphate-based speckles can be used. Consequently there was the problem of providing a suitable coloured detergent speckle which show a uniform, bright colour whilst comprising only a low percentage of pigment or dye, which granules remain stable as to colour, which are low in attrition and non, or low, dusting, which are based on a functional base material, which have a suitable bulk density as to avoid segregation from the detergent powder upon handling/storage and which are non-caking and dissolve fast in the washing liquor.
- The present invention provides coloured detergent speckles satisfying most of the above requirements in the form of granular alkali metal silicate which has been coated with a colourant i.e. a pigment or dye.
- Preferably the alkali metal silicate is sodium silicate, more preferably metasilicate and/or disilicate.
- Silicates have the functions of improving the washing effect and of corrosion inhibitor in detergent composition and consequently are a functional additive. Especially preferred are silicate hydrates as the base material for the speckles according to the present invention and sodium silicate penta- and/or hexahydrate give optimal results. In view of the well-known high alkalinity of alkali metal silicates it was quite unexpected that these silicates could serve as the base material of uniformly, bright coloured of a deep hue and especially colour-stable detergent speckles.
- Although it is recommended that the base material for the speckles consists substantially of sodium silicate it is, however, also possible to use as the base material for the speckles a mixture of materials in which at least 50% of the dry weight consists ot alkali metal silicate, the remainder being other inorganic materials like eg. zeolite, sodium sulfate or sodium phosphate if the latter can be tolerated in the eventual detergent composition.
- The coloured silicate granules according to the present invention usually have an average particle size of 0.2 - 2mm, preferably from 0.8 to 1.6 mm, diameter. Granules with an spherical shape have advantages and then the diameter is taken to determine the size. Of course the actual size of the speckles desired depends on that of the detergent powder in which the speckles are incorporated.
- The colourant, i.e. dye or pigment, which forms a coating on the alkali metal silicate granules is normally present in an amount of 0.1 to 2.0% (w.w.) of the granules. The colourant usually is a commercially available dye and compounds like Monastral Blue and Monastral Green + Unidispers Blue (ex CIBA-Geigy) are preferred. (Monastral dyes are ex ICI, England.)
- The coloured detergent speckles are usually incorporated in detergent powders in a level between 0.1 - 5%, preferably between 0.2 and 2.0%, by weight of the total detergent composition.
- The invention extends particularly to the use of sodium silicate having Na₂O:SiO₂ ratios from 1:1.2 to 1:3.3, preferably 1:1.5 to 1:3.0. The higher ratios are generally less preferred because of slower solution. The granules of alkali metal silicate can be prepared by a number of suitable procedures, for example metasilicate (Na₂O:Silica ratio 1:1) can be granulated in a rotary barrel as described in GB 1149859 (Baker-Holloway). Silicates, for example Sodium disilicate, can be prepared in compacted form of increased bulk density by use of the procedures described in US 3875282 (Stauffer Chemical Co= and US 3931036 (PQ).
- The use of silicates in compacted form is particularly valuable for speckles intended for the higher density detergent powder compositions, that is having a bulk density above 700 g/l, preferably above 800 g/l. Sodium disilicate can be prepared with a bulk density between 700 and 900 g/l by compaction between rollers. Sodium metasilicate can be prepared with a bulk density between 880 and 1,000 g/l using granulation in a rotary barrel. At the lower density ranges the use of a binder, eg. silicate solution, may be necessary to provide integrity in the compacted mass obtained by twin rollers.
- Traditionally detergent speckles are manufactured by a number of methods. One method involved the spray-drying of a special coloured slurry but the obvious disadvantage is that thorough cleaning is required before normal detergent powder can be produced again. Another method involved spraying a coloured solution onto a spray-dried detergent powder, but this requires, as the previous method, a large amount of coloured solution. Also it has been suggested to spray onto granules a solution of a colourant that also comprises a hydratable salt, preferably a warm and concentrated solution, to facilitate subsequent crystallisation. For zeolite containing detergent compositions this method was found not quite practical because a high percentage of colourant was required.
- The coloured detergent speckles according to the present invention, which are based on alkali metal silicate, can be prepared by spraying under suitable conditions a solution of a colourant on granular alkali metal silicate, which is kept in constant motion so as to avoid caking. This can be done e.g. by carrying out the operation in a fluidized bed, or in a mixer, followed by drying while keeping the granules in constant motion. Suitable equipment for this technique comprises fluidized beds, nozzles for the coloured liquid, for hot and cool air, Tellschig*-type mixers consisting of rotating drums and fitted with a spray-nozzle, Loedige-type mixers consisting of fixed drums with an internal scraper fitted with a spray-nozzle, Nauta*-mixers of a type consisting of a conical vessel with a rotating scraper fitted with a spray-nozzle etc. (*stands for tradename).
- It is preferred to carry out the process in 4 steps to wit: pre-heating the granules, spraying on the colour, drying and cooling. The amount of dye solution or pigment suspension sprayed on the alkali metal silicate granules normally lies between 0.1 and 5.0% by weight, preferably between 0.5 - 2.0%, calculated on the alkali metal silicate.
- The particle size distribution of the starting granules determines the size of the coloured speckles and most alkali metal silicate granules are available in various, often uniform or narrow particle size ranges which can be chosen dependent on the size desired in the detergent composition.
- The solution which is sprayed onto the granular alkali metal silicate materiai usually contains from 0.05 to 50% of colourant preferably completely dissolved. Of course there is also the limitation of the solubility of e.g. the dye in the solvent to be observed. Water is preferred as the solvent but it is sometimes advantageous to use (aqueous) methanol to increase the solubility of the dye.
- The quantity of liquid sprayed onto the granules is normally between 0.1 and 5%, preferably between 0.5 and 2%, by weight calculated on the silicate and spraying normally is completed within a few minutes to half an hour, 2 to 10 minutes is typical.
- Very good results were obtained by pre-heating the alkali metal silicate granules before starting spraying with colourant solution. In any case it should be avoided to heat the alkali metal silicate granules to a temperature above their melting points, which is, in the case of sodium metasilicate pentahydrate, around 72°C. The temperature of the gas (air) blown onto the still wet granules normally varies between 25 and 70, preferably between 30 and 40°C. In order to ensure that certain silicate hydrates are substantially formed or retained it is necessary to monitor the water content of the granules during the drying operation. The percentage of water in the granule also determines its bulk density. Cooling whilst keeping the detergent speckles in constant movement also helps solidification of the surface and to prevent caking.
- The detergent speckles so obtained are distinctive, of uniform colour, resistant to attrition and have virtually the same particle size distribution as the alkali metal silicate starting granules have.
- The use of alkali metal silicates as a core for speckles is particularly efficient because, for one or more of the reasons,
- i) silicates are an active component of detergent compositions and thus no superfluous ingredients are introduced,
- ii) the silicate cores are utilised in a form in which they would, in any case, be added to a powder composition,
- iii) the silicate speckles dissolve rapidly so as to provide rapid dissolution and dilution of the surface colourant,
- iv) the silicate surface does not absorb the colourant, so that the latter is used efficiently, but retains the colourant so that it does not become dispersed throughout the powder,
- v) the silicate speckles have a uniform and acceptable appearance, and
- vi) they can be prepared with a bulk density suitable for the higher density powders.
- The invention is further described and illustrated in the following examples.
- 1.5 kg sodium metasilicate pentahydrate granules with a particle size between 0.2 and 1.2 mm was placed in a Loedige mixer of 5 litres. The mixer was switched on and the contents were pre-heated to 35 - 45°C by blowing in hot air with a temperature of 50°C. An aqueous solution containing 25% by weight of Monastral Blue was sprayed onto the granules for 5 minutes. The amount of solution sprayed onto the granules was 1% by weight calculated on the metasilicate. Consequently only 0.25% of dye was used relative to the metasilicate. Drying was also carried out at a temperature of 35-45°C for a period of 20 minutes. The water content of the metasilicate was monitored during the drying and kept at around 43% by weight. The detergent speckles were then cooled to 20°C by blowing in cool air. The detergent speckles thus obtained showed excellent brightness, a deep hue, were uniformly coloured, colour-stable and the original particle size distribution had substantially been retained. Whe mixed in a detergent powder at a level of 1% by weight they imparted an excellent consumer appeal to the product.
- Sodium disilicate (Na₂O:SiO₂ ratio of 1:2) was spray dried to provide granules.
- These were fed to a two roller press by a feed screw and compressed to a thin, ca 1mm, sheet under pressure. The sheet was then broken up by passage between intermeshing toothed wheels and sieved to provide a granular product having particle size distribution between 0.3 and 1.2 mm. The product had a bulk density of about 850 g/litre.
- These granules were coated with Monastral blue using the process described in Example 1 but using a 50% aqueous suspension of the pigment to provide a coating level of 0.25% by weight of silicate. This product was then used as speckles in a detergent formulation.
Claims (10)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
AT89303091T ATE102647T1 (en) | 1988-03-30 | 1989-03-29 | PROCESS FOR PRODUCTION OF A GRANULATED COLORED ALKALI SILICATE. |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP88200604 | 1988-03-30 | ||
EP88200604 | 1988-03-30 |
Publications (2)
Publication Number | Publication Date |
---|---|
EP0336635A1 true EP0336635A1 (en) | 1989-10-11 |
EP0336635B1 EP0336635B1 (en) | 1994-03-09 |
Family
ID=8199773
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP89303091A Revoked EP0336635B1 (en) | 1988-03-30 | 1989-03-29 | Process for preparing a coloured granular alkali metal silicate |
Country Status (5)
Country | Link |
---|---|
EP (1) | EP0336635B1 (en) |
JP (1) | JPH01299898A (en) |
AU (1) | AU3223389A (en) |
DE (1) | DE68913575T2 (en) |
ZA (1) | ZA892357B (en) |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0737739A2 (en) * | 1995-04-13 | 1996-10-16 | The Procter & Gamble Company | Process for making a detergent particle |
WO1997033965A1 (en) * | 1996-03-14 | 1997-09-18 | Henkel Kommanditgesellschaft Auf Aktien | Process and device for producing colour-flecked powdered bulk material |
WO2000027980A1 (en) * | 1998-11-06 | 2000-05-18 | The Procter & Gamble Company | Speckle particles and compositions containing the speckle particles |
EP1113068A2 (en) * | 1999-12-16 | 2001-07-04 | Clariant GmbH | Granular layered alkali silicate compound |
US6545147B1 (en) | 1999-09-10 | 2003-04-08 | Clariant Gmbh | Bleaching-active metal complexes |
WO2007096052A1 (en) * | 2006-02-25 | 2007-08-30 | Unilever Plc | Shading dye granule its use in a detergent formulation and process to make it |
US20150105312A1 (en) * | 2010-05-28 | 2015-04-16 | Milliken & Company | Colored Speckles For Use In Granular Detergents |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
AU2771792A (en) * | 1992-03-31 | 1993-11-08 | Kyowa Hakko Kogyo Co. Ltd. | Novel cosmetic |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3679610A (en) * | 1968-07-30 | 1972-07-25 | Philadelphia Quartz Co | Tinted granules |
DE2632367A1 (en) * | 1975-07-23 | 1977-02-17 | Procter & Gamble | GRANULATED COLORED PARTICLES |
DE2626383A1 (en) * | 1976-06-12 | 1977-12-22 | Baerle & Co Chem Fab Van | Sodium silicate hydrate prodn. - by adding an insoluble pigment to the solution prior to crystallisation |
EP0060728A1 (en) * | 1981-03-18 | 1982-09-22 | Unilever Plc | Process for manufacturing detergent speckles |
Family Cites Families (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
BE549160A (en) * | 1956-04-23 | |||
BE791891A (en) * | 1971-11-26 | 1973-05-24 | Procter & Gamble | Washing and cleaning compsns, to give bluing action - whasing and cleaning compsns, to give bluing action |
DE2744753C2 (en) * | 1977-10-05 | 1986-08-28 | Joh. A. Benckiser Gmbh, 6700 Ludwigshafen | Process for the production of granules |
-
1989
- 1989-03-29 JP JP1075264A patent/JPH01299898A/en active Pending
- 1989-03-29 DE DE68913575T patent/DE68913575T2/en not_active Expired - Fee Related
- 1989-03-29 AU AU32233/89A patent/AU3223389A/en not_active Abandoned
- 1989-03-29 EP EP89303091A patent/EP0336635B1/en not_active Revoked
- 1989-03-30 ZA ZA892357A patent/ZA892357B/en unknown
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3679610A (en) * | 1968-07-30 | 1972-07-25 | Philadelphia Quartz Co | Tinted granules |
DE1938756B2 (en) * | 1968-07-30 | 1978-09-14 | Philadelphia Quartz Co., Philadelphia, Pa. (V.St.A.) | Porous, rapidly soluble product based on hydrated, crystalline sodium silicate |
DE2632367A1 (en) * | 1975-07-23 | 1977-02-17 | Procter & Gamble | GRANULATED COLORED PARTICLES |
DE2626383A1 (en) * | 1976-06-12 | 1977-12-22 | Baerle & Co Chem Fab Van | Sodium silicate hydrate prodn. - by adding an insoluble pigment to the solution prior to crystallisation |
EP0060728A1 (en) * | 1981-03-18 | 1982-09-22 | Unilever Plc | Process for manufacturing detergent speckles |
Non-Patent Citations (1)
Title |
---|
CHEMICAL ABSTRACTS * |
Cited By (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0737739A2 (en) * | 1995-04-13 | 1996-10-16 | The Procter & Gamble Company | Process for making a detergent particle |
EP0737739A3 (en) * | 1995-04-13 | 1998-08-26 | The Procter & Gamble Company | Process for making a detergent particle |
WO1997033965A1 (en) * | 1996-03-14 | 1997-09-18 | Henkel Kommanditgesellschaft Auf Aktien | Process and device for producing colour-flecked powdered bulk material |
WO2000027980A1 (en) * | 1998-11-06 | 2000-05-18 | The Procter & Gamble Company | Speckle particles and compositions containing the speckle particles |
US6545147B1 (en) | 1999-09-10 | 2003-04-08 | Clariant Gmbh | Bleaching-active metal complexes |
EP1113068A2 (en) * | 1999-12-16 | 2001-07-04 | Clariant GmbH | Granular layered alkali silicate compound |
EP1113068A3 (en) * | 1999-12-16 | 2001-12-19 | Clariant GmbH | Granular layered alkali silicate compound |
WO2007096052A1 (en) * | 2006-02-25 | 2007-08-30 | Unilever Plc | Shading dye granule its use in a detergent formulation and process to make it |
US20150105312A1 (en) * | 2010-05-28 | 2015-04-16 | Milliken & Company | Colored Speckles For Use In Granular Detergents |
US11649417B2 (en) | 2010-05-28 | 2023-05-16 | Milliken & Company | Colored speckles for use in granular detergents |
Also Published As
Publication number | Publication date |
---|---|
DE68913575T2 (en) | 1994-06-16 |
EP0336635B1 (en) | 1994-03-09 |
DE68913575D1 (en) | 1994-04-14 |
ZA892357B (en) | 1990-12-28 |
AU3223389A (en) | 1989-10-05 |
JPH01299898A (en) | 1989-12-04 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US3989635A (en) | Process for improving granular detergents | |
TW200524B (en) | ||
US4488972A (en) | Bentonite agglomerates | |
JPH01318098A (en) | Powder detergent and production thereof | |
HU215705B (en) | Detergent component containing anionic surfactant and process for its preparation | |
CH648590A5 (en) | FREE-FLOWING, SPRAY-DRIED CUPBALLS. | |
EP0336635B1 (en) | Process for preparing a coloured granular alkali metal silicate | |
US4510066A (en) | Retarding setting of crutcher slurry for manufacturing base beads for detergent compositions | |
JPH0445560B2 (en) | ||
US4434068A (en) | Process for manufacturing detergent speckles | |
JPH0326795A (en) | Zeolite aggregation process and product | |
US4699729A (en) | Process for manufacturing bentonite-containing particulate fabric softening detergent composition | |
KR100572242B1 (en) | Method of preparing sodium percarbonate | |
CA2091474C (en) | Preparation of granular compositions | |
US4851137A (en) | Process for manufacturing bentonite agglomerates | |
US4526702A (en) | Process for manufacturing bentonite-containing particulate fabric softening detergent composition | |
US4767546A (en) | Fabric softening bentonite agglomerates for use in laundry detergents | |
US5744639A (en) | Granular alkali metal nitrilotriacetate | |
US4746445A (en) | Process for manufacturing bentonite agglomerates | |
US3761416A (en) | Composite particles and process for preparing same | |
US5998663A (en) | Granular alkali metal nitrilotriacetate | |
AU666249B2 (en) | Granulation process | |
CA2152090A1 (en) | Granulation process | |
GB2029854A (en) | A process for the production of finely agglomerated detergents | |
US4425253A (en) | Cogranulate of alkali metal silicate and alkali metal polyphosphate, and process for making it |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PUAI | Public reference made under article 153(3) epc to a published international application that has entered the european phase |
Free format text: ORIGINAL CODE: 0009012 |
|
AK | Designated contracting states |
Kind code of ref document: A1 Designated state(s): AT BE CH DE ES FR GB GR IT LI NL SE |
|
17P | Request for examination filed |
Effective date: 19891028 |
|
17Q | First examination report despatched |
Effective date: 19910624 |
|
RAP3 | Party data changed (applicant data changed or rights of an application transferred) |
Owner name: UNILEVER N.V. Owner name: UNILEVER PLC |
|
RTI1 | Title (correction) | ||
GRAA | (expected) grant |
Free format text: ORIGINAL CODE: 0009210 |
|
AK | Designated contracting states |
Kind code of ref document: B1 Designated state(s): AT BE CH DE ES FR GB GR IT LI NL SE |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: SE Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 19940309 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: GB Payment date: 19940309 Year of fee payment: 6 |
|
REF | Corresponds to: |
Ref document number: 102647 Country of ref document: AT Date of ref document: 19940315 Kind code of ref document: T |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: NL Payment date: 19940331 Year of fee payment: 6 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: FR Payment date: 19940413 Year of fee payment: 6 |
|
REF | Corresponds to: |
Ref document number: 68913575 Country of ref document: DE Date of ref document: 19940414 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: AT Payment date: 19940418 Year of fee payment: 6 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: DE Payment date: 19940425 Year of fee payment: 6 Ref country code: CH Payment date: 19940425 Year of fee payment: 6 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: BE Payment date: 19940428 Year of fee payment: 6 |
|
ITF | It: translation for a ep patent filed | ||
ET | Fr: translation filed | ||
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: GR Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 19940610 Ref country code: ES Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 19940610 |
|
PLBI | Opposition filed |
Free format text: ORIGINAL CODE: 0009260 |
|
26 | Opposition filed |
Opponent name: HENKEL KOMMANDITGESELLSCHAFT AUF AKTIEN Effective date: 19941130 |
|
NLR1 | Nl: opposition has been filed with the epo |
Opponent name: HENKEL KOMMANDITGESELLSCHAFT AUF AKTIEN |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: GB Effective date: 19950329 Ref country code: AT Effective date: 19950329 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: LI Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 19950331 Ref country code: CH Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 19950331 Ref country code: BE Effective date: 19950331 |
|
BERE | Be: lapsed |
Owner name: UNILEVER N.V. Effective date: 19950331 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: NL Effective date: 19951001 |
|
GBPC | Gb: european patent ceased through non-payment of renewal fee |
Effective date: 19950329 |
|
REG | Reference to a national code |
Ref country code: CH Ref legal event code: PL |
|
NLV4 | Nl: lapsed or anulled due to non-payment of the annual fee |
Effective date: 19951001 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: DE Effective date: 19951201 |
|
RDAG | Patent revoked |
Free format text: ORIGINAL CODE: 0009271 |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: PATENT REVOKED |
|
REG | Reference to a national code |
Ref country code: FR Ref legal event code: ST |
|
27W | Patent revoked |
Effective date: 19951203 |