EP0478684B1 - Detergent additive granulate and detergent - Google Patents

Detergent additive granulate and detergent Download PDF

Info

Publication number
EP0478684B1
EP0478684B1 EP90910607A EP90910607A EP0478684B1 EP 0478684 B1 EP0478684 B1 EP 0478684B1 EP 90910607 A EP90910607 A EP 90910607A EP 90910607 A EP90910607 A EP 90910607A EP 0478684 B1 EP0478684 B1 EP 0478684B1
Authority
EP
European Patent Office
Prior art keywords
granulate
detergent
enzyme
detergent additive
photobleaching
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 - Lifetime
Application number
EP90910607A
Other languages
German (de)
French (fr)
Other versions
EP0478684A1 (en
Inventor
Per Falholt
Erik Kjaer Markussen
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Novo Nordisk AS
Original Assignee
Novo Nordisk AS
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Novo Nordisk AS filed Critical Novo Nordisk AS
Publication of EP0478684A1 publication Critical patent/EP0478684A1/en
Application granted granted Critical
Publication of EP0478684B1 publication Critical patent/EP0478684B1/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • 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
    • C11D3/16Organic compounds
    • C11D3/38Products with no well-defined composition, e.g. natural products
    • C11D3/386Preparations containing enzymes, e.g. protease or amylase
    • C11D3/38672Granulated or coated enzymes
    • 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
    • C11D3/16Organic compounds
    • C11D3/38Products with no well-defined composition, e.g. natural products
    • C11D3/386Preparations containing enzymes, e.g. protease or amylase
    • 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
    • C11D17/0039Coated compositions or coated components in the compositions, (micro)capsules
    • 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
    • C11D3/0005Other compounding ingredients characterised by their effect
    • C11D3/0063Photo- activating compounds

Definitions

  • the concept of incorporation of a photobleaching agent in a detergent is known, reference being made to e.g. DE-A-3430773, EP-A-119746, and EP-A-87833.
  • the photobleaching agent is inactive if not exposed to UV light, and thus, under normal conditions, the photobleaching agent will first be activated and function as a bleaching agent when the clean laundry is dried in the open. This is a clear advantage over the detergents with a normal bleach, which will function as a bleaching agent already in the washing solution and thus damage sensitive detergent additives, especially enzymes.
  • photobleaching agents in detergents in solid form are not without problems, though.
  • particles of pure photobleaching agent or particles of detergent additives, which contains photobleaching agents at the surface thereof will tend to adhere to the laundry due to a selective adhesion ability of the photobleaching agent to the laundry, and also such photobleaching agent will tend to stay with the laundry without being dissolved during the washing process.
  • Most photobleaching agents possess a very intense color, and such photobleaching agents will create a most undesirable staining of the laundry.
  • the photobleaching agent is colorless, the above indicated attachment thereof to the laundry during the washing process will create an uneven concentration of photobleaching agent on the laundry, and in that case an uneven overbleaching action will take place when the laundry is dried in the open.
  • the detergent additive granulate according to the invention is a co-granulate containing at least one enzyme and at least one photobleaching agent, the co-granulate being coated.
  • the photobleaching agent can be any photobleaching agent, e.g. Tinolux BBS, vide the following examples, zinc phthalocyanine sulfonate (ZPS), and aluminum phthalocyanine sulfonate (APS).
  • Tinolux BBS zinc phthalocyanine sulfonate
  • ZPS zinc phthalocyanine sulfonate
  • APS aluminum phthalocyanine sulfonate
  • Tinolux and the later indicated materials Arbocel, Speswhite, and Glascol are trade marks.
  • the detergent additive granulate according to the invention will fulfil the above objective in an especially advantageous manner, if produced by means of a drum granulator, as will later be described in more detail.
  • the detergent additive granulate can and will usually contain other components besides the components listed above, provided that these components do not damage the enzyme and/or the photobleaching agent.
  • aqueous fabric washing detergent which can contain both enzymes and a photobleaching agent.
  • this detergent is aqueous, and the above problem, which is solved according to the invention, does not appear at all in relation to aqueous detergents, which exhibit other problems, e.g. stability problems.
  • EP-A-119.746 describes a detergent powder which contains both photobleach and enzyme.
  • the first step during the production of this washing powder is the formation of the aqueous crutcher slurry, consisting of surfactants, builders, fillers, and a solution of the photobleach.
  • This crutcher slurry is spray-dried, whereby the so-called base powder is formed.
  • the enzyme which may optionally be added vide page 4, line 29 in EP-A-119.746) has to be added as enzyme containing particles separate from the base powder, due to the fact that the enzyme activity in the base powder would be reduced severely or lost completely, if the enzyme was added to the crutcher solution.
  • the EP-A-119.746 contains enzyme free, photobleaching agent containing particles and photobleaching agent free enzyme containing particles. It has been found that the problem of staining and overbleaching is not completely solved in relation to this prior art washing powder.
  • DE-A-28 13 198 describes a bleaching agent which contains a special photoactivator.
  • This bleaching agent is produced by co-granulation of all constituents of the bleaching agent to a co-granulate or by granulation of a single constituent on a basis detergent component, whereas according to the invention two sensitive constituents of the detergent are selected, i.e. the enzyme and the photobleaching agent, and co-granulated.
  • the detergent additive granulate according to the invention can be produced by co-granulation in many ways, e.g. as indicated in the following.
  • the photobleaching agent is added as an aqueous solution, preferably as part of the granulation water.
  • the usual coating agents may be used, e.g. the coating agents described in DK-A-0121/88, DK-A-1377/88, and DK-A-378/88.
  • the enzyme is one or more of the enzymes protease, amylase, lipase, cellulase, oxidase, and amidase. These are the most common enzymes used in the detergent additive.
  • detergent additive granulate according to the invention between 2 and 40% w/w of cellulose fibres are incorporated into the granulate.
  • a granulate of this kind can be produced according to US-A-4,106,991 (Novo Nordisk A/S, Denmark). In this manner a dust free granulate is obtained which can easily be produced in an industrial scale.
  • the invention comprises a detergent which contains the detergent additive granulate according to the invention.
  • the concentration of the detergent additive is between 0.05 and 5% w/w. In this manner the object of the invention is fulfilled, and also, the photobleaching effect is fully satisfactory.
  • Example 1 In the following the production of the detergent additive granulate according to the invention is illustrated in Examples 1, 4, 5, 7, 9, and 10, and the use of the detergent additive granulate is illustrated in Example 11.
  • a powder mixture containing a proteolytic enzyme and with the following composition 8.0 kg of SAVINASE® with an activity of 36.1 KNPU/g 6.0 kg of fibrous cellulose Arbocel BC 200 1.6 kg of kaolin, Speswhite ECCI 2.4 kg of carbohydrate binder 20.6 kg of finely ground sodium sulphate is transferred to a 130 liter Lodige mixer FM 130 and granulated with 9.7 kg of a granulation liquid made up by mixing of 2.0 kg of Tinolux BBS (liquid), Ciba-Geigy 0.9 kg of carbohydrate binder 7.0 kg of water all other conditions during the granulation being identical to Example 1 in US-A-4.106.991 (Novo Nordisk A/S, Denmark).
  • KNPU is an activity unit for proteolytic activity, described in the document AF 220/1-GB
  • KLU is an activity unit for lipolytic activity, described in the document AF 95/5
  • CSU is an activity unit for cellulolytic activity, described in the document AF 187/3
  • KNU is an activity unit for amylolytic activity, described in the document AF 207/1, whereby all the cited documents are available on request from Novo Nordisk, Novo Allé, DK-2880 Bagsvaerd, Denmark.
  • Tinolux BBS is a photobleaching agent, which is a derivative of tetrabenzo-tetraazaporphine.
  • the moist granulate is dried on a fluid bed to a water content below 1%, and the sieve fraction of the granulate between 300 ⁇ m and 900 ⁇ m is taken out as a product.
  • This product is coated with 6.2% of polyethylene glycol (PEG 4000) and 10% of kaolin (Speswhite, ECC) by means of the method described in Example 22 in US-A-4.106.991 (Novo Nordisk A/S, Denmark).
  • the granulate is further provided with a film coating consisting of 170 ppm of duasynic acid green and 0.25% of hydroxypropyl cellulose.
  • the final preparation exhibited a proteolytic activity of 5.7 KNPU/g.
  • a powder mixture containing a lipolytic enzyme and with the following composition 0.75 kg of LIPOLASE® with an activity of 860 KLU/g 2.25 kg of fibrous cellulose Arbocel BC 200 1.50 kg of bentonite ECCI ASB350 0.90 kg of carbohydrate binder 8,90 kg of finely ground sodium sulphate is transferred to a 50 liter Lödige mixer FM 50 and granulated with 3.4 kg of a granulation liquid made up by mixing of 0.7 kg of Tinolux BBS 0.7 kg of carbohydrate binder 2.0 kg of water
  • the granulation is carried out as described in Example 1, except for the size of the mixer.
  • the granulate is dried and sifted as described in Example 1, whereby a granulate with an activity of 31.2 KLU/g is obtained.
  • a powder mixture containing a cellulolytic enzyme and with the following composition 3.00 kg of cellulase with an activity of 5340 CSU/g 2.25 kg of fibrous cellulose Arbocel BC 200 0.60 kg of kaolin ECCI Speswhite 0.60 kg of carbohydrate binder 8,85 kg of finely ground sodium sulphate is transferred to a 50 liter Lödige mixer FM 50 and granulated with 3.4 kg of a granulation liquid made up by mixing of 0.83 kg of Tinolux BBS 0.30 kg of carbohydrate binder 3.00 kg of water
  • the granulation is carried out as described in Example 1, except for the size of the mixer.
  • the granulate is dried and sifted as described in Example 1.
  • Example 2 1 kg of dry sifted (300-1000 ⁇ m) granulate produced as described in Example 2 is coated in a 5 liter Lödige mixer according to the method described in US-A-4,106,991 (Novo Nordisk A/S, Denmark), example 22.
  • Example 4 1 kg of dry sifted (300-1000 ⁇ m) granulate produced as described in Example 3 is coated as described in Example 4.
  • Example 6 5 kg of a Tinolux/bentonite coated granulate produced as described in Example 6 is further coated with 100 g of bentonite and 45 g of Glascol LS22P (dry matter) by spraying with an emulsion/suspension consisting of 100 g of bentonite ASB 350 100 g of Glascol LS22P (45% microemulsion) 500 g of water by means of the same fluidized bed coating technique as described in Example 6.
  • Example 8 5 kg of a Tinolux coated granulate produced as described in Example 8 is further coated with 200 g of bentonite and 135 g of Glascol LS22P (dry matter) by spraying with an emulsion/suspension consisting of 200 g of bentonite ASB 350 300 g of Glascol LS22P (45% microemulsion) 1000 g of water by means of the same fluidized bed coating technique as described in Example 6.
  • a powder composition containing an amylolytic enzyme and with the following composition is prepared for extrusion according to Example 4 in US-A-4,661,452 (Novo Nordisk A/S, Denmark).
  • 0.500 kg of BAN with an activity of 4900 KNU/g 0.100 kg of titanium dioxide 0.275 kg of a carbohydrate binder 0.500 kg of calcium carbonate, Sturcal L 0.350 kg of anhydrous calcium sulphate 0.125 kg of sodium carboxymethyl cellulose, Hercules 7H 2.725 kg of finely ground sodium sulphate by spraying with 600 g Tinolux BBS containing 100 g of PVP K30 and finally spraying the moist mixture with 200 g of coconut monoethanol amide.
  • the hot (55°C) moist mixture is extruded using a pellet press type extruder (Simon-Heesen type Monoroll Labor).
  • a pellet press type extruder Simon-Heesen type Monoroll Labor.
  • the original Simon-Heesen pellet die with 8 mm holes is equipped with a screen plate with 0.8 mm holes on the inside, which screen is supported by the die.
  • the extrudate After extrusion the extrudate is allowed to cool by blowing cold air through it. After cooling to room temperature it is transferred to the Marumerizer®, which breaks the extrudate to a short sized noodle like product, which is compact and exhibits a well rounded surface. Finally the product is dried in a fludized bed drier.
  • the product is coated with a protective coating as described in example 22 of US-A-4,106,991 (Novo Nordisk A/S, Denmark) or in WO-A-89/08694 (Novo Nordisk A/S, Denmark) or in WO-A-89/08695 (Novo Nordisk A/S, Denmark).
  • This example is a spotting example illustrating the use of the detergent additive granulate according to the invention.
  • Granules from Example 1 are added to a solution of a standard powder detergent in a jar. A piece of white cotton textile is placed on the bottom of the jar. The spotting from the granules on the white textile is evaluated after 1 minute according to the grades shown in the legend.

Abstract

The detergent additive granulate is a cogranulate containing at least one enzyme and at least one photobleaching agent. If a detergent, a component of which is such detergent additive granulate, is used for laundering, the photobleaching agent will not tend to adhere selectively to the laundry during the initial washing process.

Description

  • The concept of incorporation of a photobleaching agent in a detergent is known, reference being made to e.g. DE-A-3430773, EP-A-119746, and EP-A-87833. The photobleaching agent is inactive if not exposed to UV light, and thus, under normal conditions, the photobleaching agent will first be activated and function as a bleaching agent when the clean laundry is dried in the open. This is a clear advantage over the detergents with a normal bleach, which will function as a bleaching agent already in the washing solution and thus damage sensitive detergent additives, especially enzymes.
  • The introduction of photobleaching agents in detergents in solid form is not without problems, though. During the initial stages of the washing process, when the solid detergent agent is introduced into the washing float, particles of pure photobleaching agent or particles of detergent additives, which contains photobleaching agents at the surface thereof, will tend to adhere to the laundry due to a selective adhesion ability of the photobleaching agent to the laundry, and also such photobleaching agent will tend to stay with the laundry without being dissolved during the washing process. Most photobleaching agents possess a very intense color, and such photobleaching agents will create a most undesirable staining of the laundry. In case the photobleaching agent is colorless, the above indicated attachment thereof to the laundry during the washing process will create an uneven concentration of photobleaching agent on the laundry, and in that case an uneven overbleaching action will take place when the laundry is dried in the open.
  • Thus, there is a need for a detergent additive in solid form comprising a photobleaching agent, whereby during the initial washing process the photobleaching agent will not tend to adhere selectively to the laundry.
  • Now, according to the invention it has been found that a detergent additive granulate of a special composition will fulfil the above objective.
  • Thus, the detergent additive granulate according to the invention is a co-granulate containing at least one enzyme and at least one photobleaching agent, the co-granulate being coated.
  • The photobleaching agent can be any photobleaching agent, e.g. Tinolux BBS, vide the following examples, zinc phthalocyanine sulfonate (ZPS), and aluminum phthalocyanine sulfonate (APS).
  • Tinolux and the later indicated materials Arbocel, Speswhite, and Glascol are trade marks.
  • The detergent additive granulate according to the invention will fulfil the above objective in an especially advantageous manner, if produced by means of a drum granulator, as will later be described in more detail.
  • The detergent additive granulate can and will usually contain other components besides the components listed above, provided that these components do not damage the enzyme and/or the photobleaching agent.
  • In GB-A-2.179.053 an aqueous fabric washing detergent is described, which can contain both enzymes and a photobleaching agent. However, this detergent is aqueous, and the above problem, which is solved according to the invention, does not appear at all in relation to aqueous detergents, which exhibit other problems, e.g. stability problems.
  • EP-A-119.746 describes a detergent powder which contains both photobleach and enzyme. The first step during the production of this washing powder is the formation of the aqueous crutcher slurry, consisting of surfactants, builders, fillers, and a solution of the photobleach. This crutcher slurry is spray-dried, whereby the so-called base powder is formed. The enzyme which may optionally be added (vide page 4, line 29 in EP-A-119.746) has to be added as enzyme containing particles separate from the base powder, due to the fact that the enzyme activity in the base powder would be reduced severely or lost completely, if the enzyme was added to the crutcher solution. Thus, the EP-A-119.746 contains enzyme free, photobleaching agent containing particles and photobleaching agent free enzyme containing particles. It has been found that the problem of staining and overbleaching is not completely solved in relation to this prior art washing powder.
  • DE-A-28 13 198 describes a bleaching agent which contains a special photoactivator. This bleaching agent is produced by co-granulation of all constituents of the bleaching agent to a co-granulate or by granulation of a single constituent on a basis detergent component, whereas according to the invention two sensitive constituents of the detergent are selected, i.e. the enzyme and the photobleaching agent, and co-granulated.
  • The detergent additive granulate according to the invention can be produced by co-granulation in many ways, e.g. as indicated in the following.
    • I. A co-granulate of the so-called T-granulate type, as described in US-A-4,106,991 (Novo Nordisk A/S, Denmark), i.e. with cellulose fibres.
    • II. A co-granulate corresponding to US-A-4,661,452 (Novo Nordisk A/S, Denmark).
    • III. A co-granulate of the core type, as described in DK-A-4368/88. In this case it is specially preferred that the photobleaching agent is part of the core and that the enzyme is part of the coating.
    • IV. A co-granulate of the type described in DK-A-4369/88. In this case the photobleaching agent is added with the concentrated enzyme solution.
    • V. A co-granulate of the so-called "Marumerizer" type, as described in GB-A-1,362,365.
    • VI. A co-granulate of the prill type.
    • VII. A co-granulate of the Sparks type, as described in WO-A-85/05288.
    • VIII. A co-granulate of the fluid bed type.
  • In all cases the photobleaching agent is added as an aqueous solution, preferably as part of the granulation water.
  • In relation to the detergent additive granulate according to the invention the usual coating agents may be used, e.g. the coating agents described in DK-A-0121/88, DK-A-1377/88, and DK-A-378/88.
  • In a preferred embodiment of the detergent additive granulate according to the invention the enzyme is one or more of the enzymes protease, amylase, lipase, cellulase, oxidase, and amidase. These are the most common enzymes used in the detergent additive.
  • In a preferred embodiment of the detergent additive granulate according to the invention between 2 and 40% w/w of cellulose fibres are incorporated into the granulate. A granulate of this kind can be produced according to US-A-4,106,991 (Novo Nordisk A/S, Denmark). In this manner a dust free granulate is obtained which can easily be produced in an industrial scale.
  • Also, the invention comprises a detergent which contains the detergent additive granulate according to the invention.
  • In a preferred embodiment of the detergent according to the invention the concentration of the detergent additive is between 0.05 and 5% w/w. In this manner the object of the invention is fulfilled, and also, the photobleaching effect is fully satisfactory.
  • In the following the production of the detergent additive granulate according to the invention is illustrated in Examples 1, 4, 5, 7, 9, and 10, and the use of the detergent additive granulate is illustrated in Example 11.
  • EXAMPLE 1
  • A powder mixture containing a proteolytic enzyme and with the following composition
       8.0 kg of SAVINASE® with an activity of 36.1 KNPU/g
       6.0 kg of fibrous cellulose Arbocel BC 200
       1.6 kg of kaolin, Speswhite ECCI
       2.4 kg of carbohydrate binder
       20.6 kg of finely ground sodium sulphate
    is transferred to a 130 liter Lodige mixer FM 130 and granulated with 9.7 kg of a granulation liquid made up by mixing of
       2.0 kg of Tinolux BBS (liquid), Ciba-Geigy
       0.9 kg of carbohydrate binder
       7.0 kg of water
    all other conditions during the granulation being identical to Example 1 in US-A-4.106.991 (Novo Nordisk A/S, Denmark).
  • KNPU is an activity unit for proteolytic activity, described in the document AF 220/1-GB, KLU is an activity unit for lipolytic activity, described in the document AF 95/5, CSU is an activity unit for cellulolytic activity, described in the document AF 187/3, and KNU is an activity unit for amylolytic activity, described in the document AF 207/1, whereby all the cited documents are available on request from Novo Nordisk, Novo Allé, DK-2880 Bagsvaerd, Denmark.
  • Tinolux BBS is a photobleaching agent, which is a derivative of tetrabenzo-tetraazaporphine.
  • The moist granulate is dried on a fluid bed to a water content below 1%, and the sieve fraction of the granulate between 300 µm and 900 µm is taken out as a product. This product is coated with 6.2% of polyethylene glycol (PEG 4000) and 10% of kaolin (Speswhite, ECC) by means of the method described in Example 22 in US-A-4.106.991 (Novo Nordisk A/S, Denmark).
  • By means of usual fluid bed techniques, the granulate is further provided with a film coating consisting of 170 ppm of duasynic acid green and 0.25% of hydroxypropyl cellulose.
  • The final preparation exhibited a proteolytic activity of 5.7 KNPU/g.
  • EXAMPLE 2
  • A powder mixture containing a lipolytic enzyme and with the following composition
       0.75 kg of LIPOLASE® with an activity of 860 KLU/g
       2.25 kg of fibrous cellulose Arbocel BC 200
       1.50 kg of bentonite ECCI ASB350
       0.90 kg of carbohydrate binder
       8,90 kg of finely ground sodium sulphate
    is transferred to a 50 liter Lödige mixer FM 50 and granulated with 3.4 kg of a granulation liquid made up by mixing of
       0.7 kg of Tinolux BBS
       0.7 kg of carbohydrate binder
       2.0 kg of water
  • The granulation is carried out as described in Example 1, except for the size of the mixer.
  • The granulate is dried and sifted as described in Example 1, whereby a granulate with an activity of 31.2 KLU/g is obtained.
  • EXAMPLE 3
  • A powder mixture containing a cellulolytic enzyme and with the following composition
       3.00 kg of cellulase with an activity of 5340 CSU/g
       2.25 kg of fibrous cellulose Arbocel BC 200
       0.60 kg of kaolin ECCI Speswhite
       0.60 kg of carbohydrate binder
       8,85 kg of finely ground sodium sulphate
    is transferred to a 50 liter Lödige mixer FM 50 and granulated with 3.4 kg of a granulation liquid made up by mixing of
       0.83 kg of Tinolux BBS
       0.30 kg of carbohydrate binder
       3.00 kg of water
  • The granulation is carried out as described in Example 1, except for the size of the mixer.
  • The granulate is dried and sifted as described in Example 1.
  • EXAMPLE 4
  • 1 kg of dry sifted (300-1000 µm) granulate produced as described in Example 2 is coated in a 5 liter Lödige mixer according to the method described in US-A-4,106,991 (Novo Nordisk A/S, Denmark), example 22.
    Figure imgb0001
  • EXAMPLE 5
  • 1 kg of dry sifted (300-1000 µm) granulate produced as described in Example 3 is coated as described in Example 4.
    Figure imgb0002
  • EXAMPLE 6
  • 5.0 kg of base granulate produced as described in US-A-4,106,991 (Novo Nordisk A/S, Denmark), example 1, except that it is based on sodium sulphate as the inert diluent, is provided with a photobleach containing layer by means of a fluidized bed spraying technique, as follows.
  • With simultaneous drying in a Glatt fluid bed coater of type WSG5 the 5 kg of base granulate is sprayed with an emulsion/suspension consisting of
       0.75 kg of Tinolux BBS
       0.50 kg of Bentonite ASB350 (ECCI)
       0.25 kg of Glascol LS22P (Styrene-acrylic copolymer, 45% microemulsion, Allied Colloids)
       2.00 kg of water,
    and with proper selected air inlet and outlet temperature and atomizing air pressure that leaves every single enzyme granulate particle coated with a layer of dry Tinolux and bentonite with Glascol as the binding agent.
  • EXAMPLE 7
  • 5 kg of a Tinolux/bentonite coated granulate produced as described in Example 6 is further coated with 100 g of bentonite and 45 g of Glascol LS22P (dry matter) by spraying with an emulsion/suspension consisting of
       100 g of bentonite ASB 350
       100 g of Glascol LS22P (45% microemulsion)
       500 g of water
    by means of the same fluidized bed coating technique as described in Example 6.
  • EXAMPLE 8
  • 5.0 kg of base granulate produced as described in US-A-4,106,991 (Novo Nordisk A/S), example 1, except that it is based on sodium sulphate as the inert diluent, is coated with a photobleach layer by means of a fluidized bed spraying technique.
  • With simultaneous drying in a Glatt fluid bed coater of type WSG5 the 5 kg of base granulate is sprayed with 0.75 kg Tinolux BBS with proper selected air inlet and outlet temperature and atomizing air pressure that leaves every single enzyme granulate particle coated with a layer of dry Tinolux photobleach.
  • EXAMPLE 9
  • 5 kg of a Tinolux coated granulate produced as described in Example 8 is further coated with 200 g of bentonite and 135 g of Glascol LS22P (dry matter) by spraying with an emulsion/suspension consisting of
       200 g of bentonite ASB 350
       300 g of Glascol LS22P (45% microemulsion)
       1000 g of water
    by means of the same fluidized bed coating technique as described in Example 6.
  • EXAMPLE 10
  • A powder composition containing an amylolytic enzyme and with the following composition is prepared for extrusion according to Example 4 in US-A-4,661,452 (Novo Nordisk A/S, Denmark).
       0.500 kg of BAN with an activity of 4900 KNU/g
       0.100 kg of titanium dioxide
       0.275 kg of a carbohydrate binder
       0.500 kg of calcium carbonate, Sturcal L
       0.350 kg of anhydrous calcium sulphate
       0.125 kg of sodium carboxymethyl cellulose, Hercules 7H
       2.725 kg of finely ground sodium sulphate
    by spraying with 600 g Tinolux BBS containing 100 g of PVP K30 and finally spraying the moist mixture with 200 g of coconut monoethanol amide.
  • The hot (55°C) moist mixture is extruded using a pellet press type extruder (Simon-Heesen type Monoroll Labor). To obtain an extrudate with a string diameter of 0.8 mm the original Simon-Heesen pellet die with 8 mm holes is equipped with a screen plate with 0.8 mm holes on the inside, which screen is supported by the die.
  • After extrusion the extrudate is allowed to cool by blowing cold air through it. After cooling to room temperature it is transferred to the Marumerizer®, which breaks the extrudate to a short sized noodle like product, which is compact and exhibits a well rounded surface. Finally the product is dried in a fludized bed drier.
  • The product is coated with a protective coating as described in example 22 of US-A-4,106,991 (Novo Nordisk A/S, Denmark) or in WO-A-89/08694 (Novo Nordisk A/S, Denmark) or in WO-A-89/08695 (Novo Nordisk A/S, Denmark).
  • Depending on formulation and extruder type products with particle shapes ranging from pure spheres to short rod like shapes can be produced. Methods for production of spheronized/marumerized products are described in GB-A-1,362,365 (Novo Nordisk A/S, Denmark) and US-A-4,661,452 (Novo Nordisk A/S, Denmark).
  • EXAMPLE 11
  • This example is a spotting example illustrating the use of the detergent additive granulate according to the invention.
  • Granules from Example 1 are added to a solution of a standard powder detergent in a jar. A piece of white cotton textile is placed on the bottom of the jar. The spotting from the granules on the white textile is evaluated after 1 minute according to the grades shown in the legend.
  • Dosage of Tinolux 0.02%
  • Figure imgb0003
  • Dosage of Tinolux 0.04%
  • Figure imgb0004
    Figure imgb0005
    Figure imgb0006

Claims (5)

  1. Detergent additive granulate which is a co-granulate containing at least one enzyme and at least one photobleaching agent, the co-granulate being coated.
  2. Detergent additive granulate according to Claim 1, wherein the enzyme is one or more of the enzymes protease, amylase, lipase, cellulase, oxidase and amidase.
  3. Detergent additive granulate according to Claims 1 to 2, wherein between 2 and 40% w/w of cellulose fibres is incorporated into the granulate.
  4. Detergent, which contains the detergent additive granulate according to Claims 1 - 3.
  5. Detergent according to Claim 4, in which the concentration of the detergent additive granulate is between 0.05 and 5% w/w.
EP90910607A 1989-06-21 1990-06-14 Detergent additive granulate and detergent Expired - Lifetime EP0478684B1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DK3062/89 1989-06-21
DK306289A DK306289D0 (en) 1989-06-21 1989-06-21 DETERGENT ADDITIVE IN GRANULATE

Publications (2)

Publication Number Publication Date
EP0478684A1 EP0478684A1 (en) 1992-04-08
EP0478684B1 true EP0478684B1 (en) 1993-12-08

Family

ID=8118654

Family Applications (1)

Application Number Title Priority Date Filing Date
EP90910607A Expired - Lifetime EP0478684B1 (en) 1989-06-21 1990-06-14 Detergent additive granulate and detergent

Country Status (16)

Country Link
EP (1) EP0478684B1 (en)
JP (1) JPH04506229A (en)
KR (1) KR920701410A (en)
AT (1) ATE98295T1 (en)
AU (1) AU641672B2 (en)
BR (1) BR9007470A (en)
DE (1) DE69005112T2 (en)
DK (2) DK306289D0 (en)
EG (1) EG19045A (en)
ES (1) ES2046788T3 (en)
MX (1) MX21242A (en)
MY (1) MY105995A (en)
NZ (1) NZ234159A (en)
PT (1) PT94439B (en)
TR (1) TR27368A (en)
WO (1) WO1990015856A1 (en)

Families Citing this family (18)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5167854A (en) * 1985-08-21 1992-12-01 The Clorox Company Encapsulated enzyme in dry bleach composition
US5376288A (en) * 1989-06-21 1994-12-27 Noro Nordisk A/S Detergent additive granulate and detergent
GB9220669D0 (en) * 1992-09-30 1992-11-11 Unilever Plc Detergent composition
DK5593D0 (en) * 1993-01-18 1993-01-18 Novo Nordisk As GRANULES
JPH10500728A (en) * 1994-05-31 1998-01-20 ノボ ノルディスク アクティーゼル スカブ Dye transfer inhibiting formulations, and detergent compositions comprising such formulations
US6410287B1 (en) 1998-10-09 2002-06-25 Kao Corporation Enzyme particles
DE19855677A1 (en) * 1998-12-02 2000-06-08 Henkel Kgaa Production of detergent granules containing brighteners
US6767882B1 (en) 1999-06-21 2004-07-27 The Procter & Gamble Company Process for producing coated detergent particles
CA2375416A1 (en) * 1999-06-21 2000-12-28 Kenji Shindo Process for producing coated detergent particles
IT1319655B1 (en) 2000-11-15 2003-10-23 Eurand Int PANCREATIC ENZYME MICROSPHERES WITH HIGH STABILITY AND RELATIVE PREPARATION METHOD.
GB2374082A (en) * 2001-04-04 2002-10-09 Procter & Gamble Particles for a detergent product
GB0314210D0 (en) 2003-06-18 2003-07-23 Unilever Plc Laundry treatment compositions
US8246950B2 (en) 2007-02-20 2012-08-21 Aptalis Pharma Limited Stable digestive enzyme compositions
WO2009109856A2 (en) 2008-03-07 2009-09-11 Axcan Pharma Inc. Method for detecting infectious parvovirus in pharmaceutical preparations
CN108187033A (en) 2010-10-01 2018-06-22 阿普塔利斯制药有限公司 The low-intensity Cotazym of enteric coating
DK2741766T3 (en) 2011-08-08 2016-01-11 Aptalis Pharma Ltd Process for dissolving solid compositions containing digestive enzymes
US10184121B2 (en) 2013-06-28 2019-01-22 Allergan Pharmaceuticals International Limited Methods for removing viral contaminants from pancreatic extracts
MX2016001593A (en) 2013-08-09 2016-09-29 Allergan Pharmaceuticals Int Ltd Digestive enzyme composition suitable for enteral administration.

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CA1075405A (en) * 1977-03-28 1980-04-15 John F. Goodman Photoactivated bleach-compositions and process
GR78065B (en) * 1982-02-19 1984-09-26 Unilever Nv
GB8304631D0 (en) * 1983-02-18 1983-03-23 Unilever Plc Detergent powder

Also Published As

Publication number Publication date
PT94439A (en) 1991-02-08
NZ234159A (en) 1992-01-29
PT94439B (en) 1997-02-28
ATE98295T1 (en) 1993-12-15
AU5960190A (en) 1991-01-08
DK306289D0 (en) 1989-06-21
BR9007470A (en) 1992-06-16
MX21242A (en) 1993-11-01
EP0478684A1 (en) 1992-04-08
DE69005112D1 (en) 1994-01-20
TR27368A (en) 1995-01-17
DE69005112T2 (en) 1994-04-14
EG19045A (en) 1994-12-30
ES2046788T3 (en) 1994-02-01
WO1990015856A1 (en) 1990-12-27
KR920701410A (en) 1992-08-11
MY105995A (en) 1995-02-28
DK0478684T3 (en) 1994-04-18
JPH04506229A (en) 1992-10-29
AU641672B2 (en) 1993-09-30

Similar Documents

Publication Publication Date Title
EP0478684B1 (en) Detergent additive granulate and detergent
US5376288A (en) Detergent additive granulate and detergent
EP0404806B1 (en) Stabilized particulate composition
EP0270608B1 (en) Coated detergent enzymes
JP2647695B2 (en) Enzyme-containing granules
US4707287A (en) Dry bleach stable enzyme composition
JP2801395B2 (en) Detergent additive granules and manufacturing method
US5324649A (en) Enzyme-containing granules coated with hydrolyzed polyvinyl alcohol or copolymer thereof
US5318714A (en) Stabilized particulate composition
EP2007863B1 (en) Granulates for a sensitive washing- or cleaning agent containing material
EP0506791B1 (en) Enzyme containing preparation and detergent containing such preparation
EP0206418B1 (en) Dry bleach and stable enzyme granular composition
US4767557A (en) Dry bleach and stable enzyme granular composition
JPH07506124A (en) granular composition
EP2209880A1 (en) Granulate of a sensitive ingredient of a washing or cleaning agent
US6656898B1 (en) Enzyme composite particles having an acidic barrier and a physical barrier coating
JPH10502114A (en) Method for producing granules containing multiple enzymes
JP2003504050A (en) Method for preparing enzyme-containing granules
SK46398A3 (en) Encapsulated bleach particles
CN1742084B (en) Stabilization of granules
US4911851A (en) Detergent compatible, dryer released fabric softening/antistatic agents
US3781228A (en) Laundry product containing enzyme
EP0680510A1 (en) Enzyme containing granulate, method for production thereof, and use thereof
CN1152334A (en) Multiple enzyme granulates and their production

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

17P Request for examination filed

Effective date: 19910930

AK Designated contracting states

Kind code of ref document: A1

Designated state(s): AT BE CH DE DK ES FR GB IT LI LU NL SE

17Q First examination report despatched

Effective date: 19930312

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 DK ES FR GB IT LI LU NL SE

REF Corresponds to:

Ref document number: 98295

Country of ref document: AT

Date of ref document: 19931215

Kind code of ref document: T

REF Corresponds to:

Ref document number: 69005112

Country of ref document: DE

Date of ref document: 19940120

REG Reference to a national code

Ref country code: ES

Ref legal event code: FG2A

Ref document number: 2046788

Country of ref document: ES

Kind code of ref document: T3

ITF It: translation for a ep patent filed

Owner name: ST. CONSUL.BREVETTUALE S.R.L.

ET Fr: translation filed
REG Reference to a national code

Ref country code: DK

Ref legal event code: T3

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: LU

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 19940630

PLBE No opposition filed within time limit

Free format text: ORIGINAL CODE: 0009261

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: NO OPPOSITION FILED WITHIN TIME LIMIT

26N No opposition filed
EAL Se: european patent in force in sweden

Ref document number: 90910607.2

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: FR

Payment date: 19960523

Year of fee payment: 7

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: GB

Payment date: 19960605

Year of fee payment: 7

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: SE

Payment date: 19960617

Year of fee payment: 7

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: ES

Payment date: 19960619

Year of fee payment: 7

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: DE

Payment date: 19960624

Year of fee payment: 7

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: BE

Payment date: 19960625

Year of fee payment: 7

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: DK

Payment date: 19960627

Year of fee payment: 7

Ref country code: AT

Payment date: 19960627

Year of fee payment: 7

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: NL

Payment date: 19960630

Year of fee payment: 7

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: CH

Payment date: 19960702

Year of fee payment: 7

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: GB

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 19970614

Ref country code: DK

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 19970614

Ref country code: AT

Effective date: 19970614

REG Reference to a national code

Ref country code: DK

Ref legal event code: EBP

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: SE

Effective date: 19970615

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: ES

Free format text: LAPSE BECAUSE OF EXPIRATION OF PROTECTION

Effective date: 19970616

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: 19970630

Ref country code: CH

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 19970630

Ref country code: BE

Effective date: 19970630

BERE Be: lapsed

Owner name: NOVO NORDISK A/S

Effective date: 19970630

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: NL

Effective date: 19980101

GBPC Gb: european patent ceased through non-payment of renewal fee

Effective date: 19970614

REG Reference to a national code

Ref country code: CH

Ref legal event code: PL

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: FR

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 19980227

EUG Se: european patent has lapsed

Ref document number: 90910607.2

NLV4 Nl: lapsed or anulled due to non-payment of the annual fee

Effective date: 19980101

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: DE

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 19980303

REG Reference to a national code

Ref country code: FR

Ref legal event code: ST

REG Reference to a national code

Ref country code: FR

Ref legal event code: ST

REG Reference to a national code

Ref country code: ES

Ref legal event code: FD2A

Effective date: 20000201

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: IT

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES;WARNING: LAPSES OF ITALIAN PATENTS WITH EFFECTIVE DATE BEFORE 2007 MAY HAVE OCCURRED AT ANY TIME BEFORE 2007. THE CORRECT EFFECTIVE DATE MAY BE DIFFERENT FROM THE ONE RECORDED.

Effective date: 20050614