EP0404806B1 - Stabilized particulate composition - Google Patents
Stabilized particulate composition Download PDFInfo
- Publication number
- EP0404806B1 EP0404806B1 EP19890903702 EP89903702A EP0404806B1 EP 0404806 B1 EP0404806 B1 EP 0404806B1 EP 19890903702 EP19890903702 EP 19890903702 EP 89903702 A EP89903702 A EP 89903702A EP 0404806 B1 EP0404806 B1 EP 0404806B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- composition
- coating
- particles
- component
- clay
- 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.)
- Expired
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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
- C11D3/0005—Other compounding ingredients characterised by their effect
- C11D3/0084—Antioxidants; Free-radical scavengers
-
- 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
- C11D3/02—Inorganic compounds ; Elemental compounds
- C11D3/12—Water-insoluble compounds
- C11D3/124—Silicon containing, e.g. silica, silex, quartz or glass beads
- C11D3/1246—Silicates, e.g. diatomaceous earth
- C11D3/1253—Layer silicates, e.g. talcum, kaolin, clay, bentonite, smectite, montmorillonite, hectorite or attapulgite
- C11D3/126—Layer silicates, e.g. talcum, kaolin, clay, bentonite, smectite, montmorillonite, hectorite or attapulgite in solid compositions
-
- 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
- C11D3/38—Products with no well-defined composition, e.g. natural products
- C11D3/386—Preparations containing enzymes, e.g. protease or amylase
- C11D3/38672—Granulated or coated enzymes
-
- 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
- C11D3/39—Organic or inorganic per-compounds
- C11D3/3902—Organic or inorganic per-compounds combined with specific additives
- C11D3/3937—Stabilising agents
-
- 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 invention relates to a particulate composition
- a particulate composition comprising:
- the invention relates to such a composition with improved stability during storage of component (1).
- the invention also relate to particles of an enzyme or an optical brightener for use in said composition and to a method of producing said composition or particles.
- Particulate detergents containing particles of an enzyme mixed with separate particles of a bleaching agent or a detergent builder are commonly used. It is know that the latter components may negatively affect the storage stability of the enzyme.
- the prior art suggests coating of the particles of the enzyme. It is know that the coating material needs to be carefully selected since it must one hand protect the enzyme and on the other hand release the component rapidly when the detergent is dissolved.
- WO 87/07292 (Novo) teaches that the use of an enteric coating on enzyme particles improves the stability in detergent with bleach; the enteric coating material dissolves at the pH of the detergent solution. However, we have found that this does not always give sufficient storage stability.
- an enzyme in a particulate composition can be stabilized in the above-mentioned mixed composition by applying a clay coating to one or both components.
- Clay coating has previously been applied to other components, e.g. bleach activator (EP 51,987), but the use of this coating to the components considered here is novel.
- the invention provides a particulate composition comprising:
- the invention also provides a particulate product comprising an enzyme for use in the above composition, characterized by having a coating containing clay.
- the invention further provides a method for producing said composition or said particulate product, wherein the particles to be coated and an aqueous dispersion of the coating agent are introduced into a fluid bed drying apparatus, whereafter the material leaving the apparatus is collected as the product.
- the invention provides a method for producing said composition or said particulate product, comprising introducing the particles to be coated and the coating agent together with water and a binder into a mixer, followed by drying.
- Typical examples of particulate compositions according to the invention are cleaning compositions, such as detergents and laundry bleaches.
- composition of the invention contains separate particles of component (1) and (2) as defined above.
- the latter end to destabilize the former during storage.
- one or both is/are coated with clay.
- the particulate composition of the invention may obviously contain more than one type of particles of component (1) and/or component (2), in which cas one or more may be coated according to the invention.
- Component (1) is an enzyme, which is commonly used in detergents.
- Detergent enzymes are generally microbial, e.g. proteases, amylases, cellulases and lipases.
- Typical examples of detergent enzymes are: proteases derived from Bacillus (e.g. from B. licheniformis , from alkalophilic strains according to US 3,723,250 or subtilisin Novo) or Fusarium (e.g. F.oxysporum ); amylase derived from Bacillus , especially B. amyloliquefaciens ( B. subtilis or B. licheniformis ; cellulase derived from Humicola , especially H. insolens ; lipase derived from Pseudomonas (e.g. Ps.
- compositions of the invention typically contain 0.005-5%, e.g. 0.01-2% and especially 0.1-1.5% by weight of particles containing component (1).
- Component (2) is a bleaching agent of the peroxy type, or a detergent builder.
- Typical bleaching agents of the peroxy type are organic and inorganic peracids and salts thereof, e.g sodium perborate, sodium percarbonate, potassium persulphate, magnesium peroxy phthalate and diperoxy dodecane dioic acid.
- Typical detergent builders are sodium or potassium salts of tripolyphosphoric acid, citric acid, zeolite, ethylenediamine tetraacetic acid (EDTA), diethylene triamine pentaacetic acid (DTPA), and nitrilo triacetic acid (NTA).
- EDTA ethylenediamine tetraacetic acid
- DTPA diethylene triamine pentaacetic acid
- NTA nitrilo triacetic acid
- the particles containing component (2) will typically be present in amounts above 0.5%, e.g. above 1% and especially above 2% by weight.
- the amount of component (2) may be more than 50%, and even more than 80%, e.g. in laundry bleaches.
- the clay used in the coating is preferably a layered clay of the smectite type, such as montmorillonite or bentonite.
- ASB e.g. ASB 350 Powder and ASB 350S Powder (ECC International Ltd., St. Austell, Cornwall, England).
- the coating material used in the invention may consist essentially of clay, or it may comprise binders, colouring agents (such as TiO2), etc.
- Conventional binders may be used, e.g. polyvinyl pyrrolidone, polyvinyl alcohol, cellulose derivatives (such as hydroxypropyl-, carboxymethyl- or methyl-cellulose) or carbohydrates (such as dextrin, starch hydrolysates, mono- and di-saccharides and sugar alcohols). If a binder is used, the amount will typically be in the range 1-30% of the coating material.
- the amount of coating material should generally be above 0.1%, preferably above 0.5% and most preferably above 2% by weight of the coated particles.
- the clay types used in the invention may be useful detergent ingredients in their own right, acting as antiredeposition agents. To obtain this effect, it is generally preferred that the amount of clay makes up 0.1-20% of the total weight of the composition of the invention.
- the clay coating applied to the enzyme according to the invention may additionally comprise an antioxidant.
- the antioxidant may be a thiosulphate, a sulphite, a bisulphite, ascorbic acid or an ascorbate, the salts being preferably sodium or ammonium salts.
- the enzyme may have an additional protective coating, e.g. consisting of or containing a low-melting wax (such as polyethyleneglycol), enteric coating according to WO 87/02979, a mono-or diglyceride or a sorbitan ester.
- a low-melting wax such as polyethyleneglycol
- enteric coating according to WO 87/02979
- a mono-or diglyceride or a sorbitan ester may both be applied to the same particles of enzyme, with either coating as the top coating.
- the additional coating may be applied to the enzyme and the clay coating to component (2).
- the particles to be coated according to the invention are preferably granulated. Granulation may be done according to methods known in the art, e.g. NL-C 167,993 (Novo), US 4,106,991 (Novo) or US 4,661,452 (Novo).
- the particle size is preferably such that at least 90% lie in the range 3-2000 ⁇ m.
- at least 90% will usually lie in the range 250-2000 tzar (standard granulate) or in the range 100-400 ⁇ m (microgranulate).
- the coating according to the invention can be applied by means of any fluid bed method, e.g. a usual fluid bed process, a Wurster bed process or a rotor bed (Glatt) process ( vide e.g. David M. Jones, "Factors to consider in fluid-bed processing", Pharmaceutical Technology, April 1985).
- the fluid bed method can be carried out batch wise or continuously.
- the coating can be applied by introducing the particles and the coating agent together with water and a binder into a mixer, followed by drying (e.g. fluid-bed drying).
- the mixer may be a Lodige mixer or any type of granulator described in US 4,106,991 at col. 4.
- the coating agent is introduced as a dry powder, and the binder as an aqueous solution or dispersion.
- the amount of water should be adjusted so as to avoid agglomeration on one hand, and avoid excessive dust on the other hand.
- the particles may be introduced first, and the coating agent and binder later, either continuously or intermittently.
- a base (uncoated) granulate of alkaline protease was prepared with the following composition:
- the granulate was prepared as described in Example 1 of US 4,106,991, using pure water as granulating agent. After drying, the granulate was sieved, and the fraction between 300 and 900 ⁇ m was collected.
- Part of the above base granulate was coated with bentonite which was sealed to the granulate surface with carbohydrate binder, as follows: 15 kg of the base granulate was introduced into a Lodige mixer FM 50. 5 kg of bentonite ASB 350 ECC was dosed continuously by the use of a self-regulating loss-in-weight feeding system into the mixer which ran at 95 rpm during the whole layering process. The feeding rate of the bentonite was 50 kg/h.
- part of the base granulate was coated with PEG as described above, to represent a prior-art coated granulate.
- Storage stability tests were carried out by adding granulate to a powder detergent with 25% perborate, storing this at 37°C and 70% relative humidity, and determining the residual protease activity. Results are expressed in percentage of initial activity. The storage tests were run in 2 series.
- results show a marked improvement of storage stability in samples coated according to the invention.
- the prior-art coating shows no improvement over the uncoated granulate.
- a base granulate oF alkaline protease was prepared and sieved as in Example 1, except that the following composition was used:
- 15 kg of the base granulate was coated with 5 kg of bentonite ASB 350 and sealed with 0.45 kg of carbohydrate binder in the following manner.
- the base granulate was introduced into a Lodige mixer FM 50.
- the coating/layering was applied with continuous mixing and alternately applying bentonite and binder solution ( 25% carbohydrate in water) in such a balanced way that the charge was neither too sticky nor contained a substantial amount of free bentonite powder.
- the actual sequences and amounts of material were:
- the granulate was finally dried to a water content below 1% and sieved to between 300 ⁇ m and 100 ⁇ m.
- a base granulate of alkaline protease prepared as in Example 1 was coated with a layer of bentonite ASB 350 and sodium thiosulphate by a conventional fluid-bed process.
- 350 g of bentonite and 350 g of sodium thiosulphate were dispersed/dissolved in water and sprayed onto 7 kg of base granulate in a Glatt WSG 5 fluid-bed with continuous layering and drying (Air inlet temperature 50°C, air outlet temperature 35°C). The process was completed by a 5 min. drying period with air inlet temperature 50°C.
- the granulate was hereafter coated with 5% glyceryl stearate/palmitate (Grindtek MSP 90, Grindsted Product) (TM) and 12.5% TiO2:kaolin as described in Example 1 for PEG.
- Example 1 Comparison of the above results with Example 1 shows that incorporation of thiosulphate and monoglyceride gives a further improvement of the storage stability obtained with bentonite coating.
- Lipase was produced according to EP 305,216 and concentrated by ultrafiltration and evaporation.
- the resulting liquid lipase concentrate had an activity of 520,000 LU/g (see EP 305,216).
- the bentonite coated lipase granulate showed 2% loss of activity after 4 days storage and 11% loss after 10 days storage.
- the base granulate showed 9% loss of activity after 4 days storage and 23% after 10 days storage.
Abstract
Description
- The invention relates to a particulate composition comprising:
- (1) particles containing an enzyme, mixed with
- (2) separate particles containing a bleaching agent of the peroxy type or a detergent builder.
- More specifically, the invention relates to such a composition with improved stability during storage of component (1).
- The invention also relate to particles of an enzyme or an optical brightener for use in said composition and to a method of producing said composition or particles.
- Particulate detergents containing particles of an enzyme mixed with separate particles of a bleaching agent or a detergent builder are commonly used. It is know that the latter components may negatively affect the storage stability of the enzyme.
- As a solution to this stability problem, the prior art suggests coating of the particles of the enzyme. It is know that the coating material needs to be carefully selected since it must one hand protect the enzyme and on the other hand release the component rapidly when the detergent is dissolved.
- As an example, WO 87/07292 (Novo) teaches that the use of an enteric coating on enzyme particles improves the stability in detergent with bleach; the enteric coating material dissolves at the pH of the detergent solution. However, we have found that this does not always give sufficient storage stability.
- Thus, we have recognized that a need exists for a composition wherein the enzyme has improved stability during storage.
- We have surprisingly found that an enzyme in a particulate composition can be stabilized in the above-mentioned mixed composition by applying a clay coating to one or both components.
- Clay coating has previously been applied to other components, e.g. bleach activator (EP 51,987), but the use of this coating to the components considered here is novel.
- Accordingly, the invention provides a particulate composition comprising:
- (1) particles containing an enzyme, mixed with
- (2) separate particles containing a bleaching agent of the peroxy type or a detergent builder,
- The invention also provides a particulate product comprising an enzyme for use in the above composition, characterized by having a coating containing clay.
- The invention further provides a method for producing said composition or said particulate product, wherein the particles to be coated and an aqueous dispersion of the coating agent are introduced into a fluid bed drying apparatus, whereafter the material leaving the apparatus is collected as the product.
- Finally, the invention provides a method for producing said composition or said particulate product, comprising introducing the particles to be coated and the coating agent together with water and a binder into a mixer, followed by drying.
- Typical examples of particulate compositions according to the invention are cleaning compositions, such as detergents and laundry bleaches.
- The composition of the invention contains separate particles of component (1) and (2) as defined above. The latter end to destabilize the former during storage. According to the invention, one or both is/are coated with clay. The particulate composition of the invention may obviously contain more than one type of particles of component (1) and/or component (2), in which cas one or more may be coated according to the invention.
- Component (1) is an enzyme, which is commonly used in detergents.
- Detergent enzymes are generally microbial, e.g. proteases, amylases, cellulases and lipases. Typical examples of detergent enzymes are: proteases derived from Bacillus (e.g. from B. licheniformis, from alkalophilic strains according to US 3,723,250 or subtilisin Novo) or Fusarium (e.g. F.oxysporum); amylase derived from Bacillus, especially B. amyloliquefaciens (B. subtilis or B. licheniformis; cellulase derived from Humicola, especially H. insolens; lipase derived from Pseudomonas (e.g. Ps. cepacia or Ps. stutzeri), Humicola (e.g. H. insolens) or Fusarium (e.g. F. oxysporum). Examples of commercial detergent enzymes are: Alcalase, Savinase, Esperase, BAN, Termamyl, Celluzyme and Lipolase (all trade names of Novo Industri A/S).
- Compositions of the invention typically contain 0.005-5%, e.g. 0.01-2% and especially 0.1-1.5% by weight of particles containing component (1).
- Component (2) is a bleaching agent of the peroxy type, or a detergent builder.
- Typical bleaching agents of the peroxy type are organic and inorganic peracids and salts thereof, e.g sodium perborate, sodium percarbonate, potassium persulphate, magnesium peroxy phthalate and diperoxy dodecane dioic acid.
- Typical detergent builders are sodium or potassium salts of tripolyphosphoric acid, citric acid, zeolite, ethylenediamine tetraacetic acid (EDTA), diethylene triamine pentaacetic acid (DTPA), and nitrilo triacetic acid (NTA).
- The particles containing component (2) will typically be present in amounts above 0.5%, e.g. above 1% and especially above 2% by weight. The amount of component (2) may be more than 50%, and even more than 80%, e.g. in laundry bleaches.
- The clay used in the coating is preferably a layered clay of the smectite type, such as montmorillonite or bentonite.
- Examples of commercially available bentonite products are ASB, e.g. ASB 350 Powder and ASB 350S Powder (ECC International Ltd., St. Austell, Cornwall, England).
- The coating material used in the invention may consist essentially of clay, or it may comprise binders, colouring agents (such as TiO₂), etc. Conventional binders may be used, e.g. polyvinyl pyrrolidone, polyvinyl alcohol, cellulose derivatives (such as hydroxypropyl-, carboxymethyl- or methyl-cellulose) or carbohydrates (such as dextrin, starch hydrolysates, mono- and di-saccharides and sugar alcohols). If a binder is used, the amount will typically be in the range 1-30% of the coating material.
- To obtain the stabilization that forms the object of the invention, the amount of coating material should generally be above 0.1%, preferably above 0.5% and most preferably above 2% by weight of the coated particles.
- The clay types used in the invention may be useful detergent ingredients in their own right, acting as antiredeposition agents. To obtain this effect, it is generally preferred that the amount of clay makes up 0.1-20% of the total weight of the composition of the invention.
- For increased protection against a bleaching agent, the clay coating applied to the enzyme according to the invention may additionally comprise an antioxidant. The antioxidant may be a thiosulphate, a sulphite, a bisulphite, ascorbic acid or an ascorbate, the salts being preferably sodium or ammonium salts.
- For increased stabilization, the enzyme may have an additional protective coating, e.g. consisting of or containing a low-melting wax (such as polyethyleneglycol), enteric coating according to WO 87/02979, a mono-or diglyceride or a sorbitan ester. This additional coating and the clay coating may both be applied to the same particles of enzyme, with either coating as the top coating. Alternatively, the additional coating may be applied to the enzyme and the clay coating to component (2).
- The particles to be coated according to the invention are preferably granulated. Granulation may be done according to methods known in the art, e.g. NL-C 167,993 (Novo), US 4,106,991 (Novo) or US 4,661,452 (Novo).
- The particle size is preferably such that at least 90% lie in the range 3-2000 µm. For a granulate, at least 90% will usually lie in the range 250-2000 tzar (standard granulate) or in the range 100-400 µm (microgranulate).
- The coating according to the invention can be applied by means of any fluid bed method, e.g. a usual fluid bed process, a Wurster bed process or a rotor bed (Glatt) process (vide e.g. David M. Jones, "Factors to consider in fluid-bed processing", Pharmaceutical Technology, April 1985). The fluid bed method can be carried out batch wise or continuously.
- Alternatively, the coating can be applied by introducing the particles and the coating agent together with water and a binder into a mixer, followed by drying (e.g. fluid-bed drying). The mixer may be a Lodige mixer or any type of granulator described in US 4,106,991 at col. 4. Conveniently, the coating agent is introduced as a dry powder, and the binder as an aqueous solution or dispersion. The amount of water should be adjusted so as to avoid agglomeration on one hand, and avoid excessive dust on the other hand. The particles may be introduced first, and the coating agent and binder later, either continuously or intermittently.
- A base (uncoated) granulate of alkaline protease was prepared with the following composition:
- 22%
- protease concentrate (SAVINASE (reg. TM of Novo Industri A/S), prepared according to US 3,723,250 at col. 12, activity 40 KNPU/g)
- 15%
- fibrous cellulose (ARBOCEL BC 200) (TM)
- 4%
- titanium dioxide
- 10%
- carbohydrate binder
- 49%
- finely ground sodium sulphate
- The granulate was prepared as described in Example 1 of US 4,106,991, using pure water as granulating agent. After drying, the granulate was sieved, and the fraction between 300 and 900 µm was collected.
- Part of the above base granulate was coated with bentonite which was sealed to the granulate surface with carbohydrate binder, as follows: 15 kg of the base granulate was introduced into a Lodige mixer FM 50. 5 kg of bentonite ASB 350 ECC was dosed continuously by the use of a self-regulating loss-in-weight feeding system into the mixer which ran at 95 rpm during the whole layering process. The feeding rate of the bentonite was 50 kg/h. Simultaneously, 0.45 kg of carbohydrate binder as a 25% solution was sprayed to bind the bentonite to the granulate surface usng a peristaltic pump and an air atomizing nozzle (atomizing pressure 19.6 N/cm²/g (2 kg/cm²/g), pumping rate 300 g/min). After layering of the bentonite, the wet coated granulate was treated for 1 min. with the granulating device as described in US 4,106,991. The velocity of the mixing device was during this period raised to 180 rev/min. The granulate was finally dried to a water content below 1% and sieved to between 300 µm and 1000 µm.
- Another sample of base granulate was coated as above except that the bentonite was type 350S, ECC. Part of this granulate was further coated by applying a solution containing 7% of polyethylene glycol and 12.5% of a 1:1 mixture of titanium dioxide and kaolin (SPESWHITE ECC) as described in example 22 of US 4,106,991.
- For comparison, part of the base granulate was coated with PEG as described above, to represent a prior-art coated granulate.
-
- The results show a marked improvement of storage stability in samples coated according to the invention. The prior-art coating shows no improvement over the uncoated granulate.
- A base granulate oF alkaline protease was prepared and sieved as in Example 1, except that the following composition was used:
- 7%
- protease concentrate (ESPERASE (reg. TM of Novo Industri A/S), prepared according to US 3,723,250 at col. 12, activity 82 KNPU/g)
- 10%
- fibrous cellulose (ARBOCEL BC 200) (TM)
- 4%
- kaolin SPESWHITE ECC (TM)
- 10%
- carbohydrate binder
- 69%
- finely ground sodium sulphate
- 15 kg of the base granulate was coated with 5 kg of bentonite ASB 350 and sealed with 0.45 kg of carbohydrate binder in the following manner. The base granulate was introduced into a Lodige mixer FM 50. The coating/layering was applied with continuous mixing and alternately applying bentonite and binder solution ( 25% carbohydrate in water) in such a balanced way that the charge was neither too sticky nor contained a substantial amount of free bentonite powder. The actual sequences and amounts of material were:
- 1. 200 g binder solution
- 2. 1670 g bentonite
- 3. 500 g binder solution
- 4. 1670 g bentonite
- 5. 500 g binder solution
- 6. 1670 g bentonite
- 7. 500 g binder solution
- 8. 2 min treatment with granulating device, mixer 180 rev/min
- 9. 150 g binder solution
- 10. 1 min treatment with granulating device, mixer 180 rev/min
- The granulate was finally dried to a water content below 1% and sieved to between 300 µm and 100 µm.
- Part of the above bentonite-coated granulate was further coated with a water-insoluble sorbitan ester of a fatty acid (FAMODAN TS, Grindsted Products) (TM) as described in Example 1 for PEG.
-
- The results show that storage stability is significantly improved by use of a bentonite coating according to the invention, and is further improved by combining this with a wax coating. The prior-art coating gives no improved stability.
- A base granulate of alkaline protease prepared as in Example 1 was coated with a layer of bentonite ASB 350 and sodium thiosulphate by a conventional fluid-bed process. 350 g of bentonite and 350 g of sodium thiosulphate were dispersed/dissolved in water and sprayed onto 7 kg of base granulate in a Glatt WSG 5 fluid-bed with continuous layering and drying (Air inlet temperature 50°C, air outlet temperature 35°C). The process was completed by a 5 min. drying period with air inlet temperature 50°C. The granulate was hereafter coated with 5% glyceryl stearate/palmitate (Grindtek MSP 90, Grindsted Product) (TM) and 12.5% TiO₂:kaolin as described in Example 1 for PEG.
-
- Comparison of the above results with Example 1 shows that incorporation of thiosulphate and monoglyceride gives a further improvement of the storage stability obtained with bentonite coating.
- Lipase was produced according to EP 305,216 and concentrated by ultrafiltration and evaporation. The resulting liquid lipase concentrate had an activity of 520,000 LU/g (see EP 305,216). The following powder components:
- 6.0
- kg fibrous cellulose ARBOCEL BC200
- 4.0
- kg kaolin SPESWHITE/ECC
- 4.2
- kg carbohydrate binder
- 24.4
- kg finely grounded sodium sulphate
- 15 kg of the base granulate was coated with 5 kg of bentonite (ASB 350) and sealed with 0,45 kg of carbohydrate binder in a manner as described in example 3. The granulate was finally dried to a water content below 1% and sieved to between 300 µm and 1000 µm.
- Storage stability tests were carried out with storage conditions as described in example 1.
- The bentonite coated lipase granulate showed 2% loss of activity after 4 days storage and 11% loss after 10 days storage.
- For comparison, the base granulate showed 9% loss of activity after 4 days storage and 23% after 10 days storage.
Claims (20)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
AT89903702T ATE73484T1 (en) | 1988-03-14 | 1989-03-13 | STABILIZED PARTICLE COMPOSITION. |
Applications Claiming Priority (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DK1377/88 | 1988-03-14 | ||
DK1378/88 | 1988-03-14 | ||
DK137788A DK137788D0 (en) | 1988-03-14 | 1988-03-14 | AS A GRANULATE PRESENTING DERTERGENTENZYM PRODUCT, PROCEDURES FOR PREPARING THEREOF, APPLICATION THEREOF AND DETERGENT CONTAINING SUCH PRODUCT |
DK137888A DK137888D0 (en) | 1988-03-14 | 1988-03-14 | STABILIZED PARTICULATE COMPOSITION |
Publications (2)
Publication Number | Publication Date |
---|---|
EP0404806A1 EP0404806A1 (en) | 1991-01-02 |
EP0404806B1 true EP0404806B1 (en) | 1992-03-11 |
Family
ID=26065676
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP19890903702 Expired EP0404806B1 (en) | 1988-03-14 | 1989-03-13 | Stabilized particulate composition |
Country Status (3)
Country | Link |
---|---|
EP (1) | EP0404806B1 (en) |
JP (1) | JP2624860B2 (en) |
WO (2) | WO1989008694A1 (en) |
Cited By (2)
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Family Cites Families (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DK130127A (en) * | 1967-10-06 | |||
US3953292A (en) * | 1974-02-01 | 1976-04-27 | Engelhard Minerals & Chemicals Corporation | Enzymes bound to heat-activated attapulgite clay |
ES8400768A1 (en) * | 1980-11-06 | 1983-11-01 | Procter & Gamble | Bleach activator compositions, preparation thereof and use in granular detergent compositions. |
GB8424812D0 (en) * | 1984-10-02 | 1984-11-07 | Unilever Plc | Enzymatic detergent composition |
US4689297A (en) * | 1985-03-05 | 1987-08-25 | Miles Laboratories, Inc. | Dust free particulate enzyme formulation |
US4707287A (en) * | 1985-06-28 | 1987-11-17 | The Procter & Gamble Company | Dry bleach stable enzyme composition |
-
1989
- 1989-03-13 EP EP19890903702 patent/EP0404806B1/en not_active Expired
- 1989-03-13 WO PCT/DK1989/000055 patent/WO1989008694A1/en unknown
- 1989-03-13 WO PCT/DK1989/000056 patent/WO1989008695A1/en active IP Right Grant
- 1989-03-13 JP JP1503949A patent/JP2624860B2/en not_active Expired - Lifetime
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0862623A2 (en) | 1995-10-06 | 1998-09-09 | Genencor International, Inc. | Microgranule for food/feed applications |
US7803604B2 (en) | 2000-07-28 | 2010-09-28 | Henkel Ag & Co. Kgaa | Amylolytic enzyme extracted from Bacillus sp. A 7-7 (DSM 12368) and washing and cleaning agents containing this novel amylolytic enzyme |
Also Published As
Publication number | Publication date |
---|---|
EP0404806A1 (en) | 1991-01-02 |
JPH03503423A (en) | 1991-08-01 |
JP2624860B2 (en) | 1997-06-25 |
WO1989008695A1 (en) | 1989-09-21 |
WO1989008694A1 (en) | 1989-09-21 |
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