CA1285508C - Dry bleach and stable enzyme granular composition - Google Patents
Dry bleach and stable enzyme granular compositionInfo
- Publication number
- CA1285508C CA1285508C CA000512635A CA512635A CA1285508C CA 1285508 C CA1285508 C CA 1285508C CA 000512635 A CA000512635 A CA 000512635A CA 512635 A CA512635 A CA 512635A CA 1285508 C CA1285508 C CA 1285508C
- Authority
- CA
- Canada
- Prior art keywords
- enzyme
- granulate
- granular composition
- weight
- alkaline buffer
- 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 - Fee Related
Links
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
- C11D3/16—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
- C11D3/3945—Organic per-compounds
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)
Abstract
DRY BLEACH AND STABLE ENZYME GRANULAR COMPOSITION
ABSTRACT
This invention relates to an enzyme and peroxyacid bleach granular composition comprising (1) a homogeneously mixed granulate of enzymes and alkaline buffer salt to protect the enzymes from deactivation when mixed with (2) a strong peroxy-acid bleach granulate. This composition can also contain detergent surface-active agents, water-soluble builder salts, and other ingredients commonly used in detergents and laundry additive products.
ABSTRACT
This invention relates to an enzyme and peroxyacid bleach granular composition comprising (1) a homogeneously mixed granulate of enzymes and alkaline buffer salt to protect the enzymes from deactivation when mixed with (2) a strong peroxy-acid bleach granulate. This composition can also contain detergent surface-active agents, water-soluble builder salts, and other ingredients commonly used in detergents and laundry additive products.
Description
~ ~28~
DRY BLEACH AND STABLE ENZYME GRA~ULAR COMPOSITION
Robert W. Herdeman s BACKGROUND OF THE INVENTION
This invention reiates to an improved dry bleach and stable en~yme granular compositions.
During the last score of years the use of enzymes, especially of microbial origin, has been more and more common. Enzymes are used in, for example, the starch in~stry to produce glucose and fructose by means of amylases, amylglucosidases and glucose isomerases. In the dairy industry a vast tonnage of rennets is used and in the detergent industry proteases are normally used as additives in the washing powders to impart a better action on proteinaceous stains on the laundry.
On July 7, 1970, C. E~. McCarty w~s granted U.S. Pat. No.
3,519,570 for enzyme-containing detergent compositions and a process for conglutination of enzymes and detergents. U.S. Pat.
No. 3,784,476, van Kampen et al., issued Jan. 8, 1974, discloses a particulate enzyme-containing detergent composition containing a detergent surface-active agent, a water soluble builder salt and discrete, shaped inorganic solids containing proteolytic or amylolytic en2ymes. It should be noted that this patent does not teach an enzyme granulate with alkaline buffer salt as defined herein (pH of 7-11 ) used in combination with a peroxyacid bleach as disclosed herein.
U.S. Pat. No. 4,106,991, Markensen et al., issued Aug. 15, 1978, discloses an improved formation for enzyme granula~es comprising enzyme, inorganic salts, a granulation binder, and finely divided cellulose fibers as 2 40~ by weight of the granulate. Optionally, a waxy substance can be employed for the granulating agent, or to coat the granulate.
The granulates so produced are reported by Markensen et al. to have a higher physical stability and a higher resistance against abrasion than granulates without cellulose fibers and, . ... . . . ..
s~
consequently, a very low dust level. Markensen et al. ~oes not disclose that use of alkaline buffer salts would tmprove the enzyme stability in the presence of peroxyacid bleach.
After the development of the granulated and coated enzymes 5 presently offered to the detergent industry, the use of the enzymes in detergents has grown steadily.
Making a storage stable mixture of enzyme containing granulates and dry peroxyacid bleach granulates is a difficult task. In spite of the fact that some commercially avaiiable enzyme 1~ granulates are advertised as "perborate bleach stable," they are weak storagewise in the presence of strong peroxyacid bleach granulates. It should be noted that peroxyacid bleach granulates are relative newcomers to the dry commercial laundry detergent and bleach markets. Tlle term "bleach" as used herein unless 15 ~therwise specified means peroxyacid bleach and the terms "per-oxyacid bleach powder" and "peroxyacid bleach granulates" are synonymous unless otherwise specified. The term "en7yme" as used hereinafter means raw enzyme, unless otherwise specified.
The term "enzyme powder" means a mixture of raw enzyme and 20 inorganic salts.
SUI~MARY OF TIIE INVENTION
This invention relates to an improved dry bleach and stable enzyme granular composition. The enzyme granulate comprises a homogeneous mixture of proteolytic or amylolytic enzyme and 25 alkaline buffer salt. The improved enzyme granulate is stable when mixed with peroxyacid bleach granulates.
OBJECTS
It is an object of the present invention to provide a dry bleach and stable enzyme granular composition. Other objeçts will 30 become apparent in the light of this disclosure.
DETAILED DESCRIPTION OF THE INVENTION
This invention relates to an improved dry bleach and stable enzyme granular composition. The enzyme granulate comprises a homogeneous mixture of proteolytic or amylolytic en2yme and 35 alkaline buffer salt. The improved enzyme granulate is stable ~ `
3551~)8 r when mixed with peroxyacid bleach granulates. The term 'igranu-lar" as used herein means the composition comprising: (1) enzyme granulates and (2) peroxyacid bleach granulates, unless otherwise specified.
This invention has an improved water-soluble enzyme granu-late containing enzymes, fillers and/or binders and an effective amount of alkaline buffer salt to protect the enzyrne from de-activation via contact with peroxyacid bleach granulate. The alkaline buffer salt has a pH of from abo~Jt 7 to about 11. The practical level of alkali buffer salt material contained in the granulate is from about 3% to about 97 . 5~ by weight of the enzyme granulate. An alkaline buffer salt material as used herein is d~fined as a material havin~ an effective amount of alkaline buffer salt and compatible inorganic salts. Some practical ratio levels of raw (proteolytic and/or amylase) enzyme to alkaline buffer salt material are from 1:4 to 1:200, preferably 1:6 to 1: 1 00 , and more preferably 1: 20 to 1: 50 .
The present invention, therefore~, provides a storage stable granular composition comprising:
(I) an enzyme granulate including a homogeneous mixture of 0.5% to 20% raw enzyme, 3% to 97.5%
alkaline buffer salt material, 2% to 40~
cellulosic filler and binder, with said enzyme having an activity of about 0.25-10 Au/gram, and (II) a peroxyacid bleach granulate, wherein said (~) and (II) have a weight ratio of from about 1:1 to about 1:1500;
wherein said alkaline buffer salt material has a pH of 30 from 7 to 11;
wherein said raw enzyme and said alkaline buffer salt material have a weight ratio of from 1:4 to 1:200; and wherein said cellulosic filler and binder of said (I) have a weight ratlo of about 1:1 to 10:1.
The improved enzyme granulate on a weight percentage basis preferably comprises:
.
`:~
355~
. .
. --.
Enz~me Granulate Levels (%) Ingredient Preferred Low High Proteolytic Enzyme 4 0.5 15 Amylase Enzyrn~ 1 0 5 Alkaline Buffer Salt Material 45 3.0 97.5 Cellulose Filler &
Binder 25 2.0 40 Optional Waxy Coating 25 o 57 The weight percentages used herein refer to the weight of the granulate being discussed, unless otherwise specified.
The improved enzyme granulate preferably is made with a raw enzyme level of from about 0.5% to about 20% (0.25 to 10 Au/gram), and more preferably from about 1% to about 10% (0.5 to 5 Au/gram) by weight of the total composition. Au equals Anson units and is a term commonly used in the trade to describe enzyme activity. The filler and binder in the enzyme granulate can have a ratio of,from 10:1 to 1:1. A practical level of cellulosic fillers in the total composition can be from about 2% to about 36%.
The stability of the alkaline buffer salt material/
enzyme granulate of -this invention is further improved with the inclusion of an antioxidant salt to the granulate. The antioxidant is preferably used at a level of from 1% to 40%, more preferably 2% to 30%. The enzyme granulate of this invention is further improved if it has a coating of alkaline buffer salt material including antioxidant with an overcoat of water-soluble nonionic waxy material over said coating.
A coating level of at least 10% alkaline buffer salt material by weight of the enzyme granulate is preferred. The waxy overcoat is preferably used at a level of 10% to 30% and more preferably 15% to 25% by weight of said granulate.
~:
~ 5~;08 ~ .
~.
_ .
Granular Compositions The improved granular composition of this invention is a mixture of peroxyacid bleach granulates, improved enzyme granulates and, optionally, other laundry active powders including so~teners, detergents, etc. Examples of powdered detergent materials are disclosed in U.S. Pat.
No. 4,404,128, B.J. Anderson, issued Sept. 13, 1983.
Examples of detergent composition and builder salts are disclosed in U.S. Pat. No. 3,784,476, van Kampen et al., issued Jan. 8, 1974. Examples of powdered peroxyacid bleach granulates are disclosed in U.S. Pat. No. 4,473,507, F.P. Bossue, issued Sept. 25, 1984! Suitable granular compositions can be formulated within the following ranges:
'~..;
~ ?~85508 Ingredient Weight %
Bleach granulate 0.5-98 Enzyme G ranu late 0 .1 -1 5 Brightener 0-3 Alkali metal builder salts~ 0-80 Anionic surfactant 2-30 Nonionic surfactant 1-10 Ammonium and sodium sulfate 0-80 Perfume 0-1 Other laundry ingredients/
additives, i.e., softeners 0-20 *Orthophosphates, pyrophosphates, tripolyphosphates, nitrilo-triacetates, ethylenediamine tetraacetates, carbonates and si l icates .
A preferred mixture is an snzyme-peroxyacid bleach granu-lar composition comprising the alkaline buffer salt protected enzyme ~ranulate of this invention and a peroxyacicl bleach granulate having a weight ratio of from 1 :1 to 1 :1500 of enzyme granulate to bleach granulate, preferably 1:3 to 1:30. Details of such a preferred mixture is disclosed below.
The Alkaline Buffer Salt Material The term "alkaline buffer salt material" as used herein means a salt having a pH of 7-11 and which provides a comparable pH
for the enzyme granulate in the presence of acidic substances for an extended period of time. Thus, the alkaline buffer salt material useful in the present invention can include any one of a number of suitable compatible inorganic salts which have a pl I of about 7-11. A pH of 8-10 is preferred. The pH of a salt is measured as a 10% solution of the salt. Some preferred alkaline buffer salts are potassium bicarbonate, potassium carbonate, tetrapotassium pyrophosphate, potassium tripolyphosphate, sodium bicarbonate and sodium carbonate. Other suitable alkaline buffer salts can be used.
~5~
The alkaline buffer salt material can constitute 97.5% of the solids in the enzyme granulate. In this case at least 2~ is cel-lulosic fibers and 0. 5% enzyme per Table 1 . However, other compatible materials can be included as part of the alkaline buffer salt material, e.g., other inorganic salts, fillers, binders, etc.
Calcium is a preferred component and can be added as calcium sulfate or calcium chloride.
The Antioxidant As used herein the term "antioxidant" means a substance that opposes oxidation or inhibits reaction provided by oxygen or peroxides. The antioxidant is an enzyme stability booster for the alkaline buffer salt enzyme granulate. The antioxidant increases the stability of the enzyme when used in conjunction with alkaline buffer salt. The preferred en~yme granulate can contain an antioxidant salt, preferably at a level of from 1-40%, and more preferably 2-30% by weight of the enzyme granlJlate. Some pre-ferred antioxidant salts are sodium sulfite, sodium bisulfite and sodium thiosulfate. Other suitable antioxidant salts can be used.
The Enzyme Granulate The enzyme granulate of the present invention has a particle size of from 100 to 160~, preferably from about 200 to about 80~, more preferably 300-500 A preferred process for making enzyme granulates of this invention comprises drum granulating an enzyme material, inor-ganic salts, a granulation binder, a liquid phase granulating agent, and finely divided cellulose fibers. In accordance with the present invention the inorganic salts are selected to include an effective amount of alkaline buffer salt material to protect the enzyme from rapid deactivation upon exposure to peroxyacid bleach granulates.
The process for the production of enzyme granulates com-prises the introduction into a drum granulator of from 2 to 40% by weight of cellulose in fibrous form, from 0 to 10% by weight of a binder as herein defined, 0 . 5% to 20% enzyme and 3% to 97 . 5%
alkaline buffer salt material in an amount which generates the intended enzyme activity in the finished granulate, a liquid phase granulating agent consisting of a waxy substance, as defined herein, and/or water, in an amount of between 5 and 70% by weight, whereby the maximum amount of waxy substance is 40% by weight and the maximum amount of water is 70% by weight, 5 whereby all percentages are referring to the total amount of dry substances, the sequence of the introduction of the different materials being arbitrary, except that at least a major part of the granulating agent is introduced after at least a substantial part of the dry substances is introduced in the granula~or, whereafter 10 the granulate, if necessary, is dried in a conventional manner, preferably in a fluid bed.
The ceilulose in fibrous form can be sawdust, pure, fibrous cellulose, cotton, or other forms of pure or impure fibrous cel-Iulose. Several brands of cellulose in fibrous form are on the 15 market, e.g., CEP~ and ARRt)CEL*, In a publication from Svenska Tramjolsfabrikerna AB, "Cepo Cellulose Powder, " it is stated that for 'Cepo S/20'*cellulose the approximate minimum fiber length is 50~, the approximate average fiber length is 16~, the approximate maximum fiber width is 50~ and the approximate 20 average fiber width is 3~ . Also, ît is stated that CEPO SS/200 cellulose has an approximate maximum fiber length of 1 50f~, an approximate average fiber length of 5,~, an approximate maximum fiber width of 4~4 and an approximate average fiber width of 2,~. Cellulose fibers with these dimensions are very well suited 25 for the purpose of the invention.
The binders usecl in the process are the binders convention-ally used in the field of granulation with a high melting point or with no melting point at all and of a nonwaxy nature, e.g., polyvinyl pyrrolidone, dextrin, polyvinylalcohol, and cellulose 30 derivatives, including for example hydroxypropyl cellulose, methyl cellulose or CMC. A granulate cannot be formed on the basis of cellulose, filler, enzyme, alkaline buffer salt material and a binder, without the use of a granulating agent, as defined below.
The term "enzyme" as used herein means raw enzyme unless 35 otherwise specified. The term "enzyme powder" means raw * Trademark (each instance) ,.. .
.~
.--~ ~ssa~
enzyme mixed with inorganic salts such as NaCI, CaCI2, etc. All enzymes can be granulated by means of said process. Prefer-ably, amylases and proteinases are granulated according to the invention. Specific examples are ALCALASE (a Bacillus licheni-formTs proteinase), ESPERASE* and SAVINASE (microbial alcaline proteinases produced according to British Pat. No. 1,243,784) and TERMAMYL ~ Baccilus licheniformis amyiase). The enzyme can be introduced into the granulator as a predried milled powder or as a solution, for example, a concentrated enzyme solution pre-10 pared by ultrafiltration, reverse osmosis or evaporation.
The granulating agent is water andlor a waxy substance.
The granulating agent is always used as a liquid phase in the granulation process; the waxy substance if present therefore is either dissolved or dispersed in the water or melted. By a "waxy 15 substance" is understood a "wax" which possesses all of the following characteristics: (1) the rnelting point is between 30 and 100C, preferably between 40 and 60C, t2) the substance is of a tough and not brittle nature, and (3) the substance possesses substantial plasticity at room temperature.
Both water and waxy substance are granulating agents, i.e., they are both active during the formation of the granulate; the waxy substance stays as a constituent in the finished granulate, whereas the majority of the water is removed during the drying.
Thus, in order to refer all amounts to the finished, dry gran-25 ulate, all percentages are calculated on the basis of total drygranulate unless otherwise specified, which means that water, one of the granulating agents, is not added to the other constituents when calculating the percentage of water, whereas the waxy substance, the other granulating agent, has to be added to the 30 other dry constituents when calculating the percentage of waxy substance. Examples of waxy substances are polyglycols, fatty alcohols, ethoxylated fatty alcohols, higher fatty acids, mono-, di- and triglycerolesters of higher fatty acids, e.g., glycerol monostearate, alkylarylethoxylates, and coconut monoethanolamide.
* Trademark ** Trademark *** Trademark **** Trademark 5~
An illustrative summary of a process used to make an enzyme granulate is:
1. Provide dry enzyme powder, cellulose fillers, alkaline buffer salt materials, binders, etc.
2, Mix the dry powders of the granulate.
DRY BLEACH AND STABLE ENZYME GRA~ULAR COMPOSITION
Robert W. Herdeman s BACKGROUND OF THE INVENTION
This invention reiates to an improved dry bleach and stable en~yme granular compositions.
During the last score of years the use of enzymes, especially of microbial origin, has been more and more common. Enzymes are used in, for example, the starch in~stry to produce glucose and fructose by means of amylases, amylglucosidases and glucose isomerases. In the dairy industry a vast tonnage of rennets is used and in the detergent industry proteases are normally used as additives in the washing powders to impart a better action on proteinaceous stains on the laundry.
On July 7, 1970, C. E~. McCarty w~s granted U.S. Pat. No.
3,519,570 for enzyme-containing detergent compositions and a process for conglutination of enzymes and detergents. U.S. Pat.
No. 3,784,476, van Kampen et al., issued Jan. 8, 1974, discloses a particulate enzyme-containing detergent composition containing a detergent surface-active agent, a water soluble builder salt and discrete, shaped inorganic solids containing proteolytic or amylolytic en2ymes. It should be noted that this patent does not teach an enzyme granulate with alkaline buffer salt as defined herein (pH of 7-11 ) used in combination with a peroxyacid bleach as disclosed herein.
U.S. Pat. No. 4,106,991, Markensen et al., issued Aug. 15, 1978, discloses an improved formation for enzyme granula~es comprising enzyme, inorganic salts, a granulation binder, and finely divided cellulose fibers as 2 40~ by weight of the granulate. Optionally, a waxy substance can be employed for the granulating agent, or to coat the granulate.
The granulates so produced are reported by Markensen et al. to have a higher physical stability and a higher resistance against abrasion than granulates without cellulose fibers and, . ... . . . ..
s~
consequently, a very low dust level. Markensen et al. ~oes not disclose that use of alkaline buffer salts would tmprove the enzyme stability in the presence of peroxyacid bleach.
After the development of the granulated and coated enzymes 5 presently offered to the detergent industry, the use of the enzymes in detergents has grown steadily.
Making a storage stable mixture of enzyme containing granulates and dry peroxyacid bleach granulates is a difficult task. In spite of the fact that some commercially avaiiable enzyme 1~ granulates are advertised as "perborate bleach stable," they are weak storagewise in the presence of strong peroxyacid bleach granulates. It should be noted that peroxyacid bleach granulates are relative newcomers to the dry commercial laundry detergent and bleach markets. Tlle term "bleach" as used herein unless 15 ~therwise specified means peroxyacid bleach and the terms "per-oxyacid bleach powder" and "peroxyacid bleach granulates" are synonymous unless otherwise specified. The term "en7yme" as used hereinafter means raw enzyme, unless otherwise specified.
The term "enzyme powder" means a mixture of raw enzyme and 20 inorganic salts.
SUI~MARY OF TIIE INVENTION
This invention relates to an improved dry bleach and stable enzyme granular composition. The enzyme granulate comprises a homogeneous mixture of proteolytic or amylolytic enzyme and 25 alkaline buffer salt. The improved enzyme granulate is stable when mixed with peroxyacid bleach granulates.
OBJECTS
It is an object of the present invention to provide a dry bleach and stable enzyme granular composition. Other objeçts will 30 become apparent in the light of this disclosure.
DETAILED DESCRIPTION OF THE INVENTION
This invention relates to an improved dry bleach and stable enzyme granular composition. The enzyme granulate comprises a homogeneous mixture of proteolytic or amylolytic en2yme and 35 alkaline buffer salt. The improved enzyme granulate is stable ~ `
3551~)8 r when mixed with peroxyacid bleach granulates. The term 'igranu-lar" as used herein means the composition comprising: (1) enzyme granulates and (2) peroxyacid bleach granulates, unless otherwise specified.
This invention has an improved water-soluble enzyme granu-late containing enzymes, fillers and/or binders and an effective amount of alkaline buffer salt to protect the enzyrne from de-activation via contact with peroxyacid bleach granulate. The alkaline buffer salt has a pH of from abo~Jt 7 to about 11. The practical level of alkali buffer salt material contained in the granulate is from about 3% to about 97 . 5~ by weight of the enzyme granulate. An alkaline buffer salt material as used herein is d~fined as a material havin~ an effective amount of alkaline buffer salt and compatible inorganic salts. Some practical ratio levels of raw (proteolytic and/or amylase) enzyme to alkaline buffer salt material are from 1:4 to 1:200, preferably 1:6 to 1: 1 00 , and more preferably 1: 20 to 1: 50 .
The present invention, therefore~, provides a storage stable granular composition comprising:
(I) an enzyme granulate including a homogeneous mixture of 0.5% to 20% raw enzyme, 3% to 97.5%
alkaline buffer salt material, 2% to 40~
cellulosic filler and binder, with said enzyme having an activity of about 0.25-10 Au/gram, and (II) a peroxyacid bleach granulate, wherein said (~) and (II) have a weight ratio of from about 1:1 to about 1:1500;
wherein said alkaline buffer salt material has a pH of 30 from 7 to 11;
wherein said raw enzyme and said alkaline buffer salt material have a weight ratio of from 1:4 to 1:200; and wherein said cellulosic filler and binder of said (I) have a weight ratlo of about 1:1 to 10:1.
The improved enzyme granulate on a weight percentage basis preferably comprises:
.
`:~
355~
. .
. --.
Enz~me Granulate Levels (%) Ingredient Preferred Low High Proteolytic Enzyme 4 0.5 15 Amylase Enzyrn~ 1 0 5 Alkaline Buffer Salt Material 45 3.0 97.5 Cellulose Filler &
Binder 25 2.0 40 Optional Waxy Coating 25 o 57 The weight percentages used herein refer to the weight of the granulate being discussed, unless otherwise specified.
The improved enzyme granulate preferably is made with a raw enzyme level of from about 0.5% to about 20% (0.25 to 10 Au/gram), and more preferably from about 1% to about 10% (0.5 to 5 Au/gram) by weight of the total composition. Au equals Anson units and is a term commonly used in the trade to describe enzyme activity. The filler and binder in the enzyme granulate can have a ratio of,from 10:1 to 1:1. A practical level of cellulosic fillers in the total composition can be from about 2% to about 36%.
The stability of the alkaline buffer salt material/
enzyme granulate of -this invention is further improved with the inclusion of an antioxidant salt to the granulate. The antioxidant is preferably used at a level of from 1% to 40%, more preferably 2% to 30%. The enzyme granulate of this invention is further improved if it has a coating of alkaline buffer salt material including antioxidant with an overcoat of water-soluble nonionic waxy material over said coating.
A coating level of at least 10% alkaline buffer salt material by weight of the enzyme granulate is preferred. The waxy overcoat is preferably used at a level of 10% to 30% and more preferably 15% to 25% by weight of said granulate.
~:
~ 5~;08 ~ .
~.
_ .
Granular Compositions The improved granular composition of this invention is a mixture of peroxyacid bleach granulates, improved enzyme granulates and, optionally, other laundry active powders including so~teners, detergents, etc. Examples of powdered detergent materials are disclosed in U.S. Pat.
No. 4,404,128, B.J. Anderson, issued Sept. 13, 1983.
Examples of detergent composition and builder salts are disclosed in U.S. Pat. No. 3,784,476, van Kampen et al., issued Jan. 8, 1974. Examples of powdered peroxyacid bleach granulates are disclosed in U.S. Pat. No. 4,473,507, F.P. Bossue, issued Sept. 25, 1984! Suitable granular compositions can be formulated within the following ranges:
'~..;
~ ?~85508 Ingredient Weight %
Bleach granulate 0.5-98 Enzyme G ranu late 0 .1 -1 5 Brightener 0-3 Alkali metal builder salts~ 0-80 Anionic surfactant 2-30 Nonionic surfactant 1-10 Ammonium and sodium sulfate 0-80 Perfume 0-1 Other laundry ingredients/
additives, i.e., softeners 0-20 *Orthophosphates, pyrophosphates, tripolyphosphates, nitrilo-triacetates, ethylenediamine tetraacetates, carbonates and si l icates .
A preferred mixture is an snzyme-peroxyacid bleach granu-lar composition comprising the alkaline buffer salt protected enzyme ~ranulate of this invention and a peroxyacicl bleach granulate having a weight ratio of from 1 :1 to 1 :1500 of enzyme granulate to bleach granulate, preferably 1:3 to 1:30. Details of such a preferred mixture is disclosed below.
The Alkaline Buffer Salt Material The term "alkaline buffer salt material" as used herein means a salt having a pH of 7-11 and which provides a comparable pH
for the enzyme granulate in the presence of acidic substances for an extended period of time. Thus, the alkaline buffer salt material useful in the present invention can include any one of a number of suitable compatible inorganic salts which have a pl I of about 7-11. A pH of 8-10 is preferred. The pH of a salt is measured as a 10% solution of the salt. Some preferred alkaline buffer salts are potassium bicarbonate, potassium carbonate, tetrapotassium pyrophosphate, potassium tripolyphosphate, sodium bicarbonate and sodium carbonate. Other suitable alkaline buffer salts can be used.
~5~
The alkaline buffer salt material can constitute 97.5% of the solids in the enzyme granulate. In this case at least 2~ is cel-lulosic fibers and 0. 5% enzyme per Table 1 . However, other compatible materials can be included as part of the alkaline buffer salt material, e.g., other inorganic salts, fillers, binders, etc.
Calcium is a preferred component and can be added as calcium sulfate or calcium chloride.
The Antioxidant As used herein the term "antioxidant" means a substance that opposes oxidation or inhibits reaction provided by oxygen or peroxides. The antioxidant is an enzyme stability booster for the alkaline buffer salt enzyme granulate. The antioxidant increases the stability of the enzyme when used in conjunction with alkaline buffer salt. The preferred en~yme granulate can contain an antioxidant salt, preferably at a level of from 1-40%, and more preferably 2-30% by weight of the enzyme granlJlate. Some pre-ferred antioxidant salts are sodium sulfite, sodium bisulfite and sodium thiosulfate. Other suitable antioxidant salts can be used.
The Enzyme Granulate The enzyme granulate of the present invention has a particle size of from 100 to 160~, preferably from about 200 to about 80~, more preferably 300-500 A preferred process for making enzyme granulates of this invention comprises drum granulating an enzyme material, inor-ganic salts, a granulation binder, a liquid phase granulating agent, and finely divided cellulose fibers. In accordance with the present invention the inorganic salts are selected to include an effective amount of alkaline buffer salt material to protect the enzyme from rapid deactivation upon exposure to peroxyacid bleach granulates.
The process for the production of enzyme granulates com-prises the introduction into a drum granulator of from 2 to 40% by weight of cellulose in fibrous form, from 0 to 10% by weight of a binder as herein defined, 0 . 5% to 20% enzyme and 3% to 97 . 5%
alkaline buffer salt material in an amount which generates the intended enzyme activity in the finished granulate, a liquid phase granulating agent consisting of a waxy substance, as defined herein, and/or water, in an amount of between 5 and 70% by weight, whereby the maximum amount of waxy substance is 40% by weight and the maximum amount of water is 70% by weight, 5 whereby all percentages are referring to the total amount of dry substances, the sequence of the introduction of the different materials being arbitrary, except that at least a major part of the granulating agent is introduced after at least a substantial part of the dry substances is introduced in the granula~or, whereafter 10 the granulate, if necessary, is dried in a conventional manner, preferably in a fluid bed.
The ceilulose in fibrous form can be sawdust, pure, fibrous cellulose, cotton, or other forms of pure or impure fibrous cel-Iulose. Several brands of cellulose in fibrous form are on the 15 market, e.g., CEP~ and ARRt)CEL*, In a publication from Svenska Tramjolsfabrikerna AB, "Cepo Cellulose Powder, " it is stated that for 'Cepo S/20'*cellulose the approximate minimum fiber length is 50~, the approximate average fiber length is 16~, the approximate maximum fiber width is 50~ and the approximate 20 average fiber width is 3~ . Also, ît is stated that CEPO SS/200 cellulose has an approximate maximum fiber length of 1 50f~, an approximate average fiber length of 5,~, an approximate maximum fiber width of 4~4 and an approximate average fiber width of 2,~. Cellulose fibers with these dimensions are very well suited 25 for the purpose of the invention.
The binders usecl in the process are the binders convention-ally used in the field of granulation with a high melting point or with no melting point at all and of a nonwaxy nature, e.g., polyvinyl pyrrolidone, dextrin, polyvinylalcohol, and cellulose 30 derivatives, including for example hydroxypropyl cellulose, methyl cellulose or CMC. A granulate cannot be formed on the basis of cellulose, filler, enzyme, alkaline buffer salt material and a binder, without the use of a granulating agent, as defined below.
The term "enzyme" as used herein means raw enzyme unless 35 otherwise specified. The term "enzyme powder" means raw * Trademark (each instance) ,.. .
.~
.--~ ~ssa~
enzyme mixed with inorganic salts such as NaCI, CaCI2, etc. All enzymes can be granulated by means of said process. Prefer-ably, amylases and proteinases are granulated according to the invention. Specific examples are ALCALASE (a Bacillus licheni-formTs proteinase), ESPERASE* and SAVINASE (microbial alcaline proteinases produced according to British Pat. No. 1,243,784) and TERMAMYL ~ Baccilus licheniformis amyiase). The enzyme can be introduced into the granulator as a predried milled powder or as a solution, for example, a concentrated enzyme solution pre-10 pared by ultrafiltration, reverse osmosis or evaporation.
The granulating agent is water andlor a waxy substance.
The granulating agent is always used as a liquid phase in the granulation process; the waxy substance if present therefore is either dissolved or dispersed in the water or melted. By a "waxy 15 substance" is understood a "wax" which possesses all of the following characteristics: (1) the rnelting point is between 30 and 100C, preferably between 40 and 60C, t2) the substance is of a tough and not brittle nature, and (3) the substance possesses substantial plasticity at room temperature.
Both water and waxy substance are granulating agents, i.e., they are both active during the formation of the granulate; the waxy substance stays as a constituent in the finished granulate, whereas the majority of the water is removed during the drying.
Thus, in order to refer all amounts to the finished, dry gran-25 ulate, all percentages are calculated on the basis of total drygranulate unless otherwise specified, which means that water, one of the granulating agents, is not added to the other constituents when calculating the percentage of water, whereas the waxy substance, the other granulating agent, has to be added to the 30 other dry constituents when calculating the percentage of waxy substance. Examples of waxy substances are polyglycols, fatty alcohols, ethoxylated fatty alcohols, higher fatty acids, mono-, di- and triglycerolesters of higher fatty acids, e.g., glycerol monostearate, alkylarylethoxylates, and coconut monoethanolamide.
* Trademark ** Trademark *** Trademark **** Trademark 5~
An illustrative summary of a process used to make an enzyme granulate is:
1. Provide dry enzyme powder, cellulose fillers, alkaline buffer salt materials, binders, etc.
2, Mix the dry powders of the granulate.
3, Wet the powder mixture with granulating agent, e.g., water or waxy melt.
4. Process ~he wet powder mixture of Step 3 in a granulating apparatus (rotating knife) until the granulate has the desired particle size distribution.
A cylindrical Lodige type mixer FM 130 DIZ (U.S. Pat. No.
3,027,102) can be used in the process for this step. The mixer is equipped with both plough shaped mixers mounted on a hori-zontal ~axial) rotating shaft and a granulating device, consis~ing of one Of more cross knives mounted on a shaft introduced into the mixer through the cylindrical wall in a direction perpendicular to the abovementioned horizontal rotating shaft (i.e., radial of the cyiinder).
A cylindrical Lodige type mixer FM 130 DIZ (U.S. Pat. No.
3,027,102) can be used in the process for this step. The mixer is equipped with both plough shaped mixers mounted on a hori-zontal ~axial) rotating shaft and a granulating device, consis~ing of one Of more cross knives mounted on a shaft introduced into the mixer through the cylindrical wall in a direction perpendicular to the abovementioned horizontal rotating shaft (i.e., radial of the cyiinder).
5. Dry in a fluidized bed the moist granulate of Step 4 until a dryness which satisfies both the requirements of enzyme stability and the requirements of free-flowing properties and mechanical strength. Usually this will correspond to a water content less than 109~, preferably less than 3~ and more preferably bone dry.
In the instances where the granulating agent is exclusively or principally a waxy substance only cooling may be required.
In the instances where the granulating agent is exclusively or principally a waxy substance only cooling may be required.
6. Optionally coating the enzyme granulate with an alkaline buffer salt coating, a waxy or some other compatible substance.
Optional Alkaline Buffer Sa!t Coating of the_Enzyme Granulate The enzyme granulate produced in the present invention can also be coated with alkaline buffer salt using any number of known apparatuses. Coating in a fluidized bed is preferred.
Examples of suitabie apparatuses and processes are disclosed in U.S. Pat. Nos. 3,196,827, Wurster and Lindlof, issued July 27, 1965; 3,253,944, Wurster, issued May 31, 1966; and 3,117,027, Lindlof and Wurster, issued Jan. 7, 1964, Trade mark ~8~
U.S. Pat. No. 3,117,027 discloses a preferred fluidized bed apparatus which can be used for coating the enzyme granulates produced in the present invention. The fluidized bed will pro-vide substantially uniformly enzyme coated granulates.
The coating process of the present invention comprises:
1. Forming an enzyme granulate having a particle size of from 100 to l 60~?, preferably 200 to 80~, with or without optional waxy coating.
2, Coating the enzyme granulate with an effective amount of alkaline buffer salt material, preferably at a level of from about 10% to about 10096 by weight of the enzyme granulate on a dry weight basis. The enzyme granulate should be surrounded by the coating and the coating should contain an effective amount of alkaline buffer salt.
The protective coating is preferably applied to the enzyme granulate as a 15g6 to 70% (preferably 20% to 50%) solids aqueous solution in a fluidized bed. The temperature range of the solu-tion can be about 60-82C (140-180F), and is preferably about 65-77C (150-170F). The air temperature of the fluidized bed is 45 to 77C for the coating/drying operation. The rate of addi-tion of the coating solution and the rate of drying are dependent on the solution concentration, temperature of air, volume, etc.
Calcium Present in Granulate and Coatin~
The enzyme granulate of this invention can be improved if it contains from about 40 to 3000 ppm of calcium calculated as cal-cium chloride. Calcium can be added to the granulate as calcium chloride or calcium sulfate powder in the granulation process or by using water containing a calcium content of 100-500 ppm, preferably 170-300 ppm, calculated as calcium chloride in the water used in the granulation and/or coating process.
Optional Waxy Coatin~ Materia!
A nonionic waxy material can be applied over the enzyme granulate or over the alkaline buffer salt coated enzyme granu-late. The practical levels of optional waxy coating material is up ~S5~8 to 57% by weight of the composition, preferably 5-30~. Examples of such waxy coatings are polyethylene glycols, fatty alcohols, ethoxylated fatty alcohols, higher fatty acids, mono-, di- and triglycerolesters of fatty acids, e.g., glycerol monostearate, 5 alkylarylethoxylates and coconut monoethanolamide. Preferred nonionic waxy substances are TAE22 ttallow alcohol condensed with 22 moles of ethylene oxide per mole of alcohol), pEG 1500-8000 (polyethyiene glycol of molecular weight 1500-8000) and palmitic acid. Other waxy coatings having a melting point of at 10 least 38C, preferably at least 50C, can also be used. For example, this waxy coating is melt~d (50-70C) and is sprayed onto the granulate in a fluidized bed where oool air (15-30~C) is applied to solidify the waxy coating.
EXAMPLE I
15A preferred enzyme granulate can be made uslng the pro-cedure outlined above using the following ingredients:
I ng redient Wt%
Proteolytic Enzyme 4 Amylase Enzyme Alkaline Buffer Salt Material1 45 Cellulose Filler2 20 Binder3 (polyvinyl pyrrolidone) 5 Waxy Overcoat (PEG 1500) 25 20% KHCO3, 5% Na25O3, 20% CaCI2/NaCI
Cellulose Powder - CEPO S20 3 Selected from polyvinyl pyrrolidone, dextrin, polyvinyl alcohols and cellulose clerivatives.
EXAMPLE l I
A 6 inch Wurster Fluidized Bed Coating Unit with a capacity of about 1 liter san be used. The enzyme granulate of Example I
can be optionally coated as follows: 800 grams of enzyme granu-35late are added to the fluid bed dryer. To this a 1,000 gram 70C
aqucous solution, containing 200 grams of potassium bicarbonate * Trade mark and 40 grams of sodiun sulfite, is sprayed on. The coated enzyme granulate is then dried at a fluid bed temperature of 75C
to contain less than 0. 596 water. The coated enzyme granulate is then removed from the fluid bed dryer and weighed to confirm 5 coating level.
About 800 grams of the alkaline buffer salt/antioxidant salt-coated enzyme granulate is then placed back into the fluid bed dryer. To this 200 grams of TAE22 are sprayed on at 55C
and allowed to cool in the dryer with air temperature 20C.
Final weight %:
Enzyme Granulate 61 . 54 Protective Coatin~:
Potassium Bicarbonate 15.38 ) Sodium Sulfite 3.08 )18.46 TAE22 Overcoating 20.00 Total 100 . 00%
The ratio of enzyme granulate to protective coating is about 3.3 to 1. The pH of the coating is 8.5.
EX AlvlPLE l l l The enzyme granulates similar to that described in Examples I or ll are dry mixed with peroxyacid bleach granulates.
Wt% G rams Peroxyacid Bleach Granulate Di pe roxydo-decanedioic Acid 20.75 Dodecanedioic Acid1 . 85 Boric Acid 22 . 75 Na25O4 28 . 06 Sodium Acid Py rophosphate 5 . 00 C1 3LAS 4 . 50 Enzyme Granulate of Example I or l l * 17 4 *2.0 Au/gram protease activity.
~ 35~
The process used to make the peroxyacid bleach granulate in Example lll is disclosed in U.S. Pat. No. 4,497,757, Beimesch and Hortel, issued Feb. 2, 1985, EXAMPLE IV
A detergent powder containing the following components:
Weight %
Diperoxydodecanedioic acid bleach granulate (Ex . I l l ) 25 Enzyme granulates of Example I or l l 2 Sodium salt of straight chain C12 alkylbenzene sulfonate 20 Sodium tripolyphosphate 35 Sodium sulfate 12 Sodium sil icate 4 Brightener Perfume capsules 0 . 3 Water, perfume Balance 5~8 EXAMPLE V
"A laundry additive containing the foliowing components:
Weight %
Diperoxydodecanedioic acid bleach granulate* 90.2 Enzyme grànulates of Example I or l l 2 Brightener and sodium siiicate 7 Perfume capsules 0. 3 Water Balance ~The peroxyacid bleach granulate of Example l l l is cut with sodium sulfate to adust peroxyacid level to about 8~ of the bleach granulate.
This invention offers an improved storage stable granular composition comprising an enzyme granulate which is storage stable with a peroxyacid bleach granulate, enabling them to be used together in a detergent or laundry additive product for 20 combined bleaching and stain removal performance.
Optional Alkaline Buffer Sa!t Coating of the_Enzyme Granulate The enzyme granulate produced in the present invention can also be coated with alkaline buffer salt using any number of known apparatuses. Coating in a fluidized bed is preferred.
Examples of suitabie apparatuses and processes are disclosed in U.S. Pat. Nos. 3,196,827, Wurster and Lindlof, issued July 27, 1965; 3,253,944, Wurster, issued May 31, 1966; and 3,117,027, Lindlof and Wurster, issued Jan. 7, 1964, Trade mark ~8~
U.S. Pat. No. 3,117,027 discloses a preferred fluidized bed apparatus which can be used for coating the enzyme granulates produced in the present invention. The fluidized bed will pro-vide substantially uniformly enzyme coated granulates.
The coating process of the present invention comprises:
1. Forming an enzyme granulate having a particle size of from 100 to l 60~?, preferably 200 to 80~, with or without optional waxy coating.
2, Coating the enzyme granulate with an effective amount of alkaline buffer salt material, preferably at a level of from about 10% to about 10096 by weight of the enzyme granulate on a dry weight basis. The enzyme granulate should be surrounded by the coating and the coating should contain an effective amount of alkaline buffer salt.
The protective coating is preferably applied to the enzyme granulate as a 15g6 to 70% (preferably 20% to 50%) solids aqueous solution in a fluidized bed. The temperature range of the solu-tion can be about 60-82C (140-180F), and is preferably about 65-77C (150-170F). The air temperature of the fluidized bed is 45 to 77C for the coating/drying operation. The rate of addi-tion of the coating solution and the rate of drying are dependent on the solution concentration, temperature of air, volume, etc.
Calcium Present in Granulate and Coatin~
The enzyme granulate of this invention can be improved if it contains from about 40 to 3000 ppm of calcium calculated as cal-cium chloride. Calcium can be added to the granulate as calcium chloride or calcium sulfate powder in the granulation process or by using water containing a calcium content of 100-500 ppm, preferably 170-300 ppm, calculated as calcium chloride in the water used in the granulation and/or coating process.
Optional Waxy Coatin~ Materia!
A nonionic waxy material can be applied over the enzyme granulate or over the alkaline buffer salt coated enzyme granu-late. The practical levels of optional waxy coating material is up ~S5~8 to 57% by weight of the composition, preferably 5-30~. Examples of such waxy coatings are polyethylene glycols, fatty alcohols, ethoxylated fatty alcohols, higher fatty acids, mono-, di- and triglycerolesters of fatty acids, e.g., glycerol monostearate, 5 alkylarylethoxylates and coconut monoethanolamide. Preferred nonionic waxy substances are TAE22 ttallow alcohol condensed with 22 moles of ethylene oxide per mole of alcohol), pEG 1500-8000 (polyethyiene glycol of molecular weight 1500-8000) and palmitic acid. Other waxy coatings having a melting point of at 10 least 38C, preferably at least 50C, can also be used. For example, this waxy coating is melt~d (50-70C) and is sprayed onto the granulate in a fluidized bed where oool air (15-30~C) is applied to solidify the waxy coating.
EXAMPLE I
15A preferred enzyme granulate can be made uslng the pro-cedure outlined above using the following ingredients:
I ng redient Wt%
Proteolytic Enzyme 4 Amylase Enzyme Alkaline Buffer Salt Material1 45 Cellulose Filler2 20 Binder3 (polyvinyl pyrrolidone) 5 Waxy Overcoat (PEG 1500) 25 20% KHCO3, 5% Na25O3, 20% CaCI2/NaCI
Cellulose Powder - CEPO S20 3 Selected from polyvinyl pyrrolidone, dextrin, polyvinyl alcohols and cellulose clerivatives.
EXAMPLE l I
A 6 inch Wurster Fluidized Bed Coating Unit with a capacity of about 1 liter san be used. The enzyme granulate of Example I
can be optionally coated as follows: 800 grams of enzyme granu-35late are added to the fluid bed dryer. To this a 1,000 gram 70C
aqucous solution, containing 200 grams of potassium bicarbonate * Trade mark and 40 grams of sodiun sulfite, is sprayed on. The coated enzyme granulate is then dried at a fluid bed temperature of 75C
to contain less than 0. 596 water. The coated enzyme granulate is then removed from the fluid bed dryer and weighed to confirm 5 coating level.
About 800 grams of the alkaline buffer salt/antioxidant salt-coated enzyme granulate is then placed back into the fluid bed dryer. To this 200 grams of TAE22 are sprayed on at 55C
and allowed to cool in the dryer with air temperature 20C.
Final weight %:
Enzyme Granulate 61 . 54 Protective Coatin~:
Potassium Bicarbonate 15.38 ) Sodium Sulfite 3.08 )18.46 TAE22 Overcoating 20.00 Total 100 . 00%
The ratio of enzyme granulate to protective coating is about 3.3 to 1. The pH of the coating is 8.5.
EX AlvlPLE l l l The enzyme granulates similar to that described in Examples I or ll are dry mixed with peroxyacid bleach granulates.
Wt% G rams Peroxyacid Bleach Granulate Di pe roxydo-decanedioic Acid 20.75 Dodecanedioic Acid1 . 85 Boric Acid 22 . 75 Na25O4 28 . 06 Sodium Acid Py rophosphate 5 . 00 C1 3LAS 4 . 50 Enzyme Granulate of Example I or l l * 17 4 *2.0 Au/gram protease activity.
~ 35~
The process used to make the peroxyacid bleach granulate in Example lll is disclosed in U.S. Pat. No. 4,497,757, Beimesch and Hortel, issued Feb. 2, 1985, EXAMPLE IV
A detergent powder containing the following components:
Weight %
Diperoxydodecanedioic acid bleach granulate (Ex . I l l ) 25 Enzyme granulates of Example I or l l 2 Sodium salt of straight chain C12 alkylbenzene sulfonate 20 Sodium tripolyphosphate 35 Sodium sulfate 12 Sodium sil icate 4 Brightener Perfume capsules 0 . 3 Water, perfume Balance 5~8 EXAMPLE V
"A laundry additive containing the foliowing components:
Weight %
Diperoxydodecanedioic acid bleach granulate* 90.2 Enzyme grànulates of Example I or l l 2 Brightener and sodium siiicate 7 Perfume capsules 0. 3 Water Balance ~The peroxyacid bleach granulate of Example l l l is cut with sodium sulfate to adust peroxyacid level to about 8~ of the bleach granulate.
This invention offers an improved storage stable granular composition comprising an enzyme granulate which is storage stable with a peroxyacid bleach granulate, enabling them to be used together in a detergent or laundry additive product for 20 combined bleaching and stain removal performance.
Claims (21)
1. A storage stable granular composition comprising:
(I) a low dust enzyme granulate including a homogeneous mixture of 0.5% to 20% raw enzyme selected from amylases and proteases and mixtures thereof, 3% to 97.5% alkaline buffer salt material selected from the group consisting of potassium bicarbonate, potassium carbonate, sodium bicarbonate, and mixtures thereof, an antioxidant inorganic salt selected from the group consisting of sodium sulfite, sodium bisulfite, sodium thiosulfate, and mixtures thereof, 2% to 40% cellulosic filler and binder, with said raw enzyme having an activity of about 0.25-10 Au/gram, said binder selected from nonwaxy polyvinyl pyrrolidone, dextrine, polyvinylalcohol, cellulose derivatives, and mixtures thereof; and (II) a peroxyacid bleach granulate, wherein said (I) and (II) have a weight ratio of from about 1:1 to about 1:1500;
wherein said alkaline buffer salt material has a pH
of above 7 to about 11;
wherein said raw enzyme and said alkaline buffer salt material have a weight ratio of from 1:4 to 1:200;
wherein said cellulosic filler and binder of said (I) have a weight ratio of about 1:1 to 10:1;
wherein said enzyme granulate (I) is made with a granulating agent selected from a waxy substance and water, said waxy substance having a melting point of from about 30°C. to about 100°C., said granulating agent being used at a level of from about 5% to about 70% by weight of dry substances, and wherein a maximum of waxy substance used is 40%.
(I) a low dust enzyme granulate including a homogeneous mixture of 0.5% to 20% raw enzyme selected from amylases and proteases and mixtures thereof, 3% to 97.5% alkaline buffer salt material selected from the group consisting of potassium bicarbonate, potassium carbonate, sodium bicarbonate, and mixtures thereof, an antioxidant inorganic salt selected from the group consisting of sodium sulfite, sodium bisulfite, sodium thiosulfate, and mixtures thereof, 2% to 40% cellulosic filler and binder, with said raw enzyme having an activity of about 0.25-10 Au/gram, said binder selected from nonwaxy polyvinyl pyrrolidone, dextrine, polyvinylalcohol, cellulose derivatives, and mixtures thereof; and (II) a peroxyacid bleach granulate, wherein said (I) and (II) have a weight ratio of from about 1:1 to about 1:1500;
wherein said alkaline buffer salt material has a pH
of above 7 to about 11;
wherein said raw enzyme and said alkaline buffer salt material have a weight ratio of from 1:4 to 1:200;
wherein said cellulosic filler and binder of said (I) have a weight ratio of about 1:1 to 10:1;
wherein said enzyme granulate (I) is made with a granulating agent selected from a waxy substance and water, said waxy substance having a melting point of from about 30°C. to about 100°C., said granulating agent being used at a level of from about 5% to about 70% by weight of dry substances, and wherein a maximum of waxy substance used is 40%.
2. The granular composition of claim 1 wherein said antioxidant to alkaline buffer salt have a weight ratio of from 10:1 to 1:50.
3. The granular composition of claim 1 or 2 wherein said (I) and said (II) have a weight ratio of 1:3 to 1:30 and said pH is 8 to 10 and said raw enzyme and said alkaline buffer salt material have a weight ratio of 1:6 to 1:100.
4. The granular composition of claim 1 or 2 wherein said raw enzyme and said alkaline buffer salt material have a weight ratio of 1:20 to 1:50.
5. The granular composition of claim 1 or 2 wherein antioxidant is present at a level of 1% to 40% by weight of said enzyme granulate and said alkaline buffer salt is present at an effective level to stabilize said enzyme from rapid deactivation in the presence of peroxyacid bleach granulate.
6. The granular composition of claim 5 wherein said antioxidant is present at a level of 2% to 30% by weight of said enzyme granulate.
7. The granular composition of claim 1 or 2 wherein said enzyme granulate contains calcium ion selected from calcium sulfate or calcium chloride at a level of 40 to 3000 ppm by weight of said enzyme granulate.
8. The granular composition of claim 1 or 2 wherein said enzyme granulate is surrounded with a coating of water-soluble nonionic wax having a melting point of at least about 38° C.
9. The granular composition of claim 8 wherein said nonionic wax is selected from the group consisting of:
fatty alcohols, polyethylene glycols, ethoxylated fatty alcohols, higher fatty acids, mono-, di- and tri-glycerolesters of fatty acids.
fatty alcohols, polyethylene glycols, ethoxylated fatty alcohols, higher fatty acids, mono-, di- and tri-glycerolesters of fatty acids.
10. The granular composition of claim 9 wherein said nonionic wax is selected from the group consisting of:
tallow alcohol condensed with 22 moles of ethylene oxide per mole of alcohol, polyethylene glycol of molecular weight 1500-8000 and palmitic acids.
tallow alcohol condensed with 22 moles of ethylene oxide per mole of alcohol, polyethylene glycol of molecular weight 1500-8000 and palmitic acids.
11. The granular composition of claim 1 or 2 wherein said enzyme granulate includes a water-soluble nonionic waxy coating at a level of from about 5% to about 57% by weight of said enzyme granulate, and has a melting point of at least 50°C.
12. The granular composition of claim 11 wherein said coating of said water-soluble nonionic waxy coating is present at a level of 10% to 30% by weight of said enzyme granulate.
13. The granular composition of claim 11 wherein said water-soluble nonionic waxy coating is present at a level of 15% to 25% by weight of said enzyme granulate.
14. The granular composition of claim 1 or 2 wherein said enzyme granulate is coated with a protective coating containing an effective amount of additional alkaline buffer salt material having a pH of from above 7 to 11;
said protective coating surrounding said enzyme granulate and providing improved enzyme stability in the presence of said peroxyacid bleach granulate.
said protective coating surrounding said enzyme granulate and providing improved enzyme stability in the presence of said peroxyacid bleach granulate.
15. The granular composition of claim 14 wherein said protective coating is from about 10% to about 67% by weight of said coated enzyme granulate.
16. The granular composition of claim 14 wherein said protective coating surrounding said enzyme granulate is from about 50% to about 80% by weight of said coated enzyme granulate,
17. The granular composition of claim 14 wherein said protective coating comprises 50% to 100% alkaline buffer salt by weight of said protective coating.
18. The granular composition of claim 14 wherein said protective coating contains 50-100% alkaline buffer salt by weight of said protective coating, and wherein said alkaline buffer salt is present at a level of from about 5% to about 10% by weight of said enzyme granulate, and wherein the balance of said protective coating is selected from antioxidants, calcium chloride and other compatible inorganic salts.
19. The granular composition of claim 14 wherein said alkaline buffer salt material protective coating having a pH of 8-10, said enzyme granulate to said protective coating has a ratio of from 4:1 to 1:1.
20. The granular composition of claim 14 wherein said protective coating is a mixture of alkaline buffer salt and antioxidant, said coating having a pH of 8 to 10.
21. The granular composition of claim 14 wherein said coating alkaline buffer salt is selected from the group consisting of potassium bicarbonate, potassium carbonate, tetrapotassium pyrophosphate, tripotassium polyphosphate, sodium bicarbonate and sodium carbonate, and mixtures thereof, said alkaline buffer salt in said protective coating is present at a level of 5% to 50% by weight of said enzyme granulate.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US75056985A | 1985-06-28 | 1985-06-28 | |
US750,569 | 1991-08-27 |
Publications (1)
Publication Number | Publication Date |
---|---|
CA1285508C true CA1285508C (en) | 1991-07-02 |
Family
ID=25018383
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CA000512635A Expired - Fee Related CA1285508C (en) | 1985-06-28 | 1986-06-27 | Dry bleach and stable enzyme granular composition |
Country Status (6)
Country | Link |
---|---|
EP (1) | EP0206418B1 (en) |
JP (1) | JPS6279296A (en) |
AU (1) | AU585031B2 (en) |
CA (1) | CA1285508C (en) |
DE (1) | DE3682443D1 (en) |
GR (1) | GR861664B (en) |
Families Citing this family (28)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4863626A (en) * | 1985-08-21 | 1989-09-05 | The Clorox Company | Encapsulated enzyme in dry bleach composition |
US5254287A (en) * | 1985-08-21 | 1993-10-19 | The Clorox Company | Encapsulated enzyme in dry bleach composition |
ATE72579T1 (en) * | 1985-08-21 | 1992-02-15 | Clorox Co | STABLE PERSACID BLEACH. |
US5093021A (en) * | 1985-08-21 | 1992-03-03 | The Clorox Company | Encapsulated enzyme in dry bleach composition |
ES2001074A6 (en) * | 1985-08-21 | 1988-04-16 | Clorox Co | Dry peracid based bleaching product. |
US5167854A (en) * | 1985-08-21 | 1992-12-01 | The Clorox Company | Encapsulated enzyme in dry bleach composition |
US4832864A (en) * | 1987-09-15 | 1989-05-23 | Ecolab Inc. | Compositions and methods that introduce variations in color density into cellulosic fabrics, particularly indigo dyed denim |
CA2015490A1 (en) * | 1989-05-01 | 1990-11-01 | Charles E. Kellner | Agglomerated peroxyacid bleach granule and process for making same |
TR25837A (en) * | 1990-05-31 | 1993-09-01 | Procter & Gamble | METHOD OF POWDERED PEROXIACID DEGREASER GRANULATED AND FOR THIS. |
GB9025673D0 (en) * | 1990-11-26 | 1991-01-09 | Unilever Plc | Detergent powders and process for preparing them |
EP0665876B1 (en) * | 1992-10-23 | 1999-03-31 | The Procter & Gamble Company | Granular detergents with protease enzyme and bleach |
KR950702625A (en) * | 1993-05-18 | 1995-07-29 | 한스 발터 라벤 | PROCESS FOR DUST-FREE ENZYME MANUFACTURE |
DE4322229A1 (en) * | 1993-07-05 | 1995-01-12 | Cognis Bio Umwelt | Enveloped enzyme preparation for detergents and cleaners |
ATE206160T1 (en) * | 1994-03-24 | 2001-10-15 | Procter & Gamble | ENZYME GRANULES |
DE4422609A1 (en) * | 1994-06-28 | 1996-01-04 | Cognis Bio Umwelt | Multi-enzyme granules |
EP0804532B1 (en) * | 1994-11-18 | 2001-01-17 | Genencor International, Inc. | Coated enzyme granules |
EP0723006A3 (en) * | 1995-01-23 | 1998-07-01 | The Procter & Gamble Company | Cleaning methods and products providing compatibilized staged release of bleach followed by enzymes |
FR2741355B1 (en) * | 1995-11-17 | 1998-12-31 | Anios Lab Sarl | COMPOSITION FOR THE TREATMENT OF OBJECTS TO BE CLEANED AND / OR DISINFECTED |
US5858952A (en) * | 1995-12-22 | 1999-01-12 | Kao Corporation | Enzyme-containing granulated product method of preparation and compositions containing the granulated product |
DE19644591A1 (en) * | 1996-10-26 | 1998-04-30 | Henkel Ecolab Gmbh & Co Ohg | Process for the production of detergents and cleaning agents containing enzymes and bleach |
DE19651446A1 (en) * | 1996-12-11 | 1998-06-18 | Henkel Kgaa | Enveloped enzyme preparation with improved solubility |
WO1999032595A1 (en) * | 1997-12-20 | 1999-07-01 | Genencor International, Inc. | Granule with hydrated barrier material |
US7425528B2 (en) | 2002-07-01 | 2008-09-16 | Novozymes A/S | Stabilization of granules |
CN1656205A (en) * | 2002-07-01 | 2005-08-17 | 诺和酶股份有限公司 | Stabilization of granules |
US7682403B2 (en) | 2004-01-09 | 2010-03-23 | Ecolab Inc. | Method for treating laundry |
EP2674475A1 (en) | 2012-06-11 | 2013-12-18 | The Procter & Gamble Company | Detergent composition |
US20170260482A1 (en) * | 2016-03-08 | 2017-09-14 | The Procter & Gamble Company | Particles including enzyme |
CN110678537B (en) | 2017-06-22 | 2021-08-10 | 埃科莱布美国股份有限公司 | Bleaching using peroxyformic acid and oxygen catalysts |
Family Cites Families (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
NL7000742A (en) * | 1970-01-19 | 1971-07-21 | Granular enzyme prepn | |
GB1590432A (en) * | 1976-07-07 | 1981-06-03 | Novo Industri As | Process for the production of an enzyme granulate and the enzyme granuate thus produced |
US4421664A (en) * | 1982-06-18 | 1983-12-20 | Economics Laboratory, Inc. | Compatible enzyme and oxidant bleaches containing cleaning composition |
ZA841401B (en) * | 1983-03-15 | 1985-10-30 | Colgate Palmolive Co | Bleaching and laundering composition free of water-soluble silicates |
GB8312185D0 (en) * | 1983-05-04 | 1983-06-08 | Unilever Plc | Bleaching and cleaning composition |
GB8321923D0 (en) * | 1983-08-15 | 1983-09-14 | Unilever Plc | Machine-dishwashing compositions |
-
1986
- 1986-06-18 EP EP19860201055 patent/EP0206418B1/en not_active Expired
- 1986-06-18 DE DE8686201055T patent/DE3682443D1/en not_active Expired - Fee Related
- 1986-06-26 GR GR861664A patent/GR861664B/en unknown
- 1986-06-27 AU AU59322/86A patent/AU585031B2/en not_active Ceased
- 1986-06-27 JP JP61151359A patent/JPS6279296A/en active Pending
- 1986-06-27 CA CA000512635A patent/CA1285508C/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
JPS6279296A (en) | 1987-04-11 |
EP0206418B1 (en) | 1991-11-13 |
GR861664B (en) | 1986-10-09 |
AU585031B2 (en) | 1989-06-08 |
DE3682443D1 (en) | 1991-12-19 |
AU5932286A (en) | 1987-01-08 |
EP0206418A2 (en) | 1986-12-30 |
EP0206418A3 (en) | 1988-11-17 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CA1285508C (en) | Dry bleach and stable enzyme granular composition | |
US4707287A (en) | Dry bleach stable enzyme composition | |
US4767557A (en) | Dry bleach and stable enzyme granular composition | |
EP0404806B1 (en) | Stabilized particulate composition | |
US3723327A (en) | Granular proteolytic enzyme composition | |
US3858854A (en) | Enzymatic detergent | |
JPH03149298A (en) | Capsulized enzyme in dry bleaching composition | |
US5318714A (en) | Stabilized particulate composition | |
US3650967A (en) | Enzymatic granules | |
EP0780466B2 (en) | Enzyme-containing granulated product, method of preparation, and compositions containing the granulated product | |
EP1124945B1 (en) | Matrix granule | |
FI66426B (en) | PARTICULAR BADKNINGSBLANDNING INNEHAOLLANDE TETRA-ACETYLETYLEN-DIAMIN | |
US3661786A (en) | Detergent compositions containing stabilized alpha-amylase | |
US3781228A (en) | Laundry product containing enzyme | |
US5783547A (en) | Enzyme granulates | |
US3823090A (en) | Production of powdered detergent | |
JP3081534B2 (en) | Enzyme-containing granules, method for producing the same, and compositions containing the same | |
NO131892B (en) | ||
JP2909888B2 (en) | Enzyme-containing granules, method for producing the same, and detergent and bleach compositions containing the same | |
US6204236B1 (en) | Enzyme granulates comprising an enzyme and an organic disulfide core | |
JPH0267399A (en) | Bleaching detergent composition | |
US3634267A (en) | Enzyme additives | |
MXPA98010048A (en) | New granulated enzyme materials comprising an enzyme and a nucleus of organic disulfide | |
MXPA98000179A (en) | Granulated compositions of e-ftalimidoperoxihexano acid |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
MKLA | Lapsed |