CA1049334A - Process for coating water soluble or water dispersible particles by means of the fluid bed technique - Google Patents
Process for coating water soluble or water dispersible particles by means of the fluid bed techniqueInfo
- Publication number
- CA1049334A CA1049334A CA205,367A CA205367A CA1049334A CA 1049334 A CA1049334 A CA 1049334A CA 205367 A CA205367 A CA 205367A CA 1049334 A CA1049334 A CA 1049334A
- Authority
- CA
- Canada
- Prior art keywords
- coating
- particles
- water soluble
- water
- coated
- 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
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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2/00—Processes or devices for granulating materials, e.g. fertilisers in general; Rendering particulate materials free flowing in general, e.g. making them hydrophobic
- B01J2/006—Coating of the granules without description of the process or the device by which the granules are obtained
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
- B01J8/1872—Details of the fluidised bed reactor
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Life Sciences & Earth Sciences (AREA)
- Combustion & Propulsion (AREA)
- Wood Science & Technology (AREA)
- Medicinal Preparation (AREA)
- Manufacturing Of Micro-Capsules (AREA)
- Detergent Compositions (AREA)
- Application Of Or Painting With Fluid Materials (AREA)
- Immobilizing And Processing Of Enzymes And Microorganisms (AREA)
- Paints Or Removers (AREA)
Abstract
ABSTRACT OF INVENTION
A process for coating water soluble or water dispersable particles by means of the fluid bed technique, comprising introduction of the particles to be coated in the fluid bed reactor and introduction of a coating fluid essentially consisting of an aqueous or substantially aqueous solution or dispersion of a macro-molecular film forming, water soluble or water dispersable coating agent by means of atomization, whereby the relative humidity of the outlet air is below 100%, and whereby the maximum size of the atomized droplets of the coating fluid does not exceed the minimum size of the particles to be coated, as well as the coated product prepared by the process.
A process for coating water soluble or water dispersable particles by means of the fluid bed technique, comprising introduction of the particles to be coated in the fluid bed reactor and introduction of a coating fluid essentially consisting of an aqueous or substantially aqueous solution or dispersion of a macro-molecular film forming, water soluble or water dispersable coating agent by means of atomization, whereby the relative humidity of the outlet air is below 100%, and whereby the maximum size of the atomized droplets of the coating fluid does not exceed the minimum size of the particles to be coated, as well as the coated product prepared by the process.
Description
~049334 This invention relates to a process for coating water soluble or water dispersible particles by means of the fluid bed technique.
It is known to coat various particulate products having a particle size of less than about 10 mm, preferably less than 1 mm, in order to minimize dust formation, e.g. enzyme containing additives for detergent compositions in powder form. I-Iowever, considerable difficulties have been experienced in performing this coating. In practice it has hitherto been usual to utilize coating agents dissolved in organic solvents rather than in water when coating water soluble particles. The organic solvents have to be evaporated and recovered at a later stage of the process and may, furthermore, create a fire hazard and environmental problems. If, on the other hand, the organic solvent is not recovered, the coating process works in an uneconomical way~ ~ ~
Also, it is known to utilize the fluid bed technique to ~ -coat various water soluble or water dispersible particles by atomization of aqueous solutions of film forming, water soluble coating agents, this process being described in Wurster's USA
patent No. 3,196,827. However, in this known process it is difficult to avoid agglomeration of the particles to be coated, and it is mentioned that this known process is only suited for particles bigger than 30 mesh (ab. 0.6 mm). Also, by using Wurster's method it is difficult to obtain thin coatings.
~ We have now found that it is possible to utilize an ; aqueous or substantially aqueous liquid for coating particulate products having a particle size of less than about 1 mm in a fluid bed process whereby particles can be coated with an extremely thin coating and without substantial danger of agglomeration.
More specifically, the process of the invention for coating water soluble or water dispersible particles by means A~ .
~ ' of the fluid be~ technique comprises introdllcing the particles to be coated in a fluid bed reactor, the mean diameter of the particles to be coated being in the ran~e of from 0.1 to 0.6 mm, and introducing a coating fluid essentially consisting of an aqueous or substantially aqueous solution or dispersion of a macromolecular film forming, water soluble or water dispersible coating agent by means of atomization, wherein the relative humi-dity of the outlet air from the fluid bed reactor is below 100% and wherein the maxirnum size of the atomized droplets of the coating fluid does not exceed the minimum size of the particles ~ be coated.
The invention also relates to a coated product which has a core of active substance formed particles having a diameter of 0.1 - 0.6 mm, which core has a thin coating of a macromolecular film forming substance.
If the maximum size of the atomized droplets of the coating fluid exceeds the minimum size of the particles to be coated, agglomeration will occur.
m us, by means of the invention agglomeration can be avoided, and it is possible to perform the coating with a layer 20 as thin as about 0.1 - 10 ~, in a preferred embodiment 0.5 corresponding to about 1% of the dry particle weight. For a given thickness of the layer of coating agent a larger amount of coating agent, calculated on the particle weight, will be used with decreasing particle size. This will appear from the following Table I.
TABLE I
Amount of coating agent, calculated as percent by weight of the particles to be coated ALCALASE P * ALCALAS E M *
Thickness of Mean diameter of Mean diameter of coatinq particles 400 ~ partic _s 700 0.5 ~ 0.8 % 0.5 %
1.0 ~ 1.5 % 0.9 %
* trademark B` - -2-~ lthough the coating produced according to the invention in a preferred embodiment is very thin it is, according to the invention, also possible to produce coatings as thick as about 100 ~, if desired The minimum size of the particles to be coated can be determined by sieve analysis, and the maximum size of the atomized droplets of coating fluid can be read from charts available from the manufacturer of the nozzle, when the viscosity of the fluid and the pressure is known.
In a preferred embodiment of the process according to the invention the water soluble or water dispersible particles to be coated contain one or more enzymes as an active ingredient, e.g. proteases, amylases, lipases or celluloses.
In another preferred embodiment of the process according to the invention the enzyme or enzymes are bacterial proteinases.
In another preferred embodiment of the process according to the invention the bacterial proteinases are precoated in order to reduce dust formation.
In another preferred embodiment of the process according to the invention the bacterial proteinases are ALCALASE P or ALCALASE M.
ALCALASE, which is a trade mark belonging to NOVO
INDUSTRI A/S, is a microbial proteinase. ALCALASE P is a prilled ALCALASE. ALCALASE M is ALCALASE which is treated by means of a Marumerizer as described in our British Patent No. 1,362,365, issued on December 4, 1974, and in our published French Patent No. 2,099,349.
In another preferred embodiment of the process according to the invention the enzyme or enzymes are bacterial or fungal carbohydrases.
_3_ In another preferred embodiment of the process according to the invention the bacterial amylases are thermally stable amylases manufactured according to sritish Patent No. 1,296,839.
In another preferred embodiment of the process according to the invention the macromolecular film forming, water soluble or water dispersible coating agent is a cellulose derivative.
In another preferred embodiment of the process according to the invention the cellulose derivative is methyl cellulose, hydroxybutylmethyl cellulose, sodium carboxymethyl cellulose, hydroxyethylmethyl cellulose or hydroxypropylmethyl cellulose.
In another preferred embodiment of the process according to the invention the macromolecular film forming, water soluble or water dispersible coating agent is a polyvinylpyrrolidone.
104g334 ~ n another preferred embodiment of the process according to the in~ention t~le macromolecular film forming, water soluble or water dispersable coating agent is a polyethylene glycol~
preferably of a molecular weight of between about 400 and about 6000.
In another preferred embodiment of the process according to the invention the macromolecular film formingJ water soluble or water dispersable coating agent is a methacrylic resin.
In another preferred embodiment of the process according to the invention the macromolecular film forming, water soluble or water dispersable coating agent is gelatine.
In another preferred embodiment of the process according to the invention the coating fluid contains a-plasticizer.
In another preferred embodiment of the`process according to the invention the plasticizer is a glycerol.
In another preferred embodiment of the process according to the invention the glycerol is used in an amount of up to 60 % of the dry weight of the coating agent, preferably in an amount of between 10 and ~0 % of the dry weight of the coating agent.
In another preferred embodiment of the process according to the invention the concentration of the macromolecular film forming, water soluble or water dispersable coating agent in the coating fluid is between 2 and 50 weight-%.
In another preferre'd embodiment of the process according to the invention the concentration of the macromolecular film forming, water soluble or water dispersable coating agent in the coating fluid is between 4 and 10 weight-%.
In another preferred embodiment of the process according to the invention the mean diameter of the particles to be coated is between 0.1 and o.6 mm.
In another preferred embodiment of the process according to the invention the mean diameter of the particles to be coated is between 0.2 and o.6 mm.
1~4~334 1ll anot~le~ p~eferred em'~o~imerlt of tile p~ocess according to the invention the thlckness o~ the coating layer is be~ween 0.1 and 10 ~.
In another preferred embodiment o~ the process-according to the invention ~he thickness of the coating layer is between 0.5 and 1 ~. -The process according to the invention can be carried outin a continuous manner as well as batchwise. However, in a pre-ferred embodiment of the invention the process is carried out batchwise. In all the following examples the process is~ carried out batchwise.
The invention also encompasses a coated product comprising coated water soluble or water dispersable particles, whenever prepared by means of the process according to the invention.
The water soluble or water dispersable particles can be of any material which, for any reason, is to be coated. Examples of materials encompassed are enzyme additives, e.g. proteolytic enzyme additives for detergents, medicaments in pellet form, e.g.
oral penicillin preparations or hygroscopic substances, e.g.
fertilizers.
Coating of the particles is carried out for various reasons, e.g. in order to minimize dust formation, to protect against ultra-violet radiation, humidity or acidity, to minimize contamination, and the like.
The coating agent can be any macromolecular film forming, water soluble or water dispersable coating agent, e.g.
METHOCEL ~ MC 15: methyl cellulose of a methoxyl DS (Degree of Substitution) of 1.64 to 1.92 and o~ a DP (Degree of Poly-merization) corresponding to viscosities from 8 cP to 10,000 cP
in a 2 % aqueous solution at 20C.
TYLOSE ~ C 10: sodium carboxymethyl cellulose of a DS from 0.4 to 1.5 and a DP from 50 to 1000.
_ . ' , 10~9334 TYLoS~ 20: methylhydroxyeth~l cellulose (or hydroxyethylmethyl cellulose) of a methoxyl DS from 1.0 to
It is known to coat various particulate products having a particle size of less than about 10 mm, preferably less than 1 mm, in order to minimize dust formation, e.g. enzyme containing additives for detergent compositions in powder form. I-Iowever, considerable difficulties have been experienced in performing this coating. In practice it has hitherto been usual to utilize coating agents dissolved in organic solvents rather than in water when coating water soluble particles. The organic solvents have to be evaporated and recovered at a later stage of the process and may, furthermore, create a fire hazard and environmental problems. If, on the other hand, the organic solvent is not recovered, the coating process works in an uneconomical way~ ~ ~
Also, it is known to utilize the fluid bed technique to ~ -coat various water soluble or water dispersible particles by atomization of aqueous solutions of film forming, water soluble coating agents, this process being described in Wurster's USA
patent No. 3,196,827. However, in this known process it is difficult to avoid agglomeration of the particles to be coated, and it is mentioned that this known process is only suited for particles bigger than 30 mesh (ab. 0.6 mm). Also, by using Wurster's method it is difficult to obtain thin coatings.
~ We have now found that it is possible to utilize an ; aqueous or substantially aqueous liquid for coating particulate products having a particle size of less than about 1 mm in a fluid bed process whereby particles can be coated with an extremely thin coating and without substantial danger of agglomeration.
More specifically, the process of the invention for coating water soluble or water dispersible particles by means A~ .
~ ' of the fluid be~ technique comprises introdllcing the particles to be coated in a fluid bed reactor, the mean diameter of the particles to be coated being in the ran~e of from 0.1 to 0.6 mm, and introducing a coating fluid essentially consisting of an aqueous or substantially aqueous solution or dispersion of a macromolecular film forming, water soluble or water dispersible coating agent by means of atomization, wherein the relative humi-dity of the outlet air from the fluid bed reactor is below 100% and wherein the maxirnum size of the atomized droplets of the coating fluid does not exceed the minimum size of the particles ~ be coated.
The invention also relates to a coated product which has a core of active substance formed particles having a diameter of 0.1 - 0.6 mm, which core has a thin coating of a macromolecular film forming substance.
If the maximum size of the atomized droplets of the coating fluid exceeds the minimum size of the particles to be coated, agglomeration will occur.
m us, by means of the invention agglomeration can be avoided, and it is possible to perform the coating with a layer 20 as thin as about 0.1 - 10 ~, in a preferred embodiment 0.5 corresponding to about 1% of the dry particle weight. For a given thickness of the layer of coating agent a larger amount of coating agent, calculated on the particle weight, will be used with decreasing particle size. This will appear from the following Table I.
TABLE I
Amount of coating agent, calculated as percent by weight of the particles to be coated ALCALASE P * ALCALAS E M *
Thickness of Mean diameter of Mean diameter of coatinq particles 400 ~ partic _s 700 0.5 ~ 0.8 % 0.5 %
1.0 ~ 1.5 % 0.9 %
* trademark B` - -2-~ lthough the coating produced according to the invention in a preferred embodiment is very thin it is, according to the invention, also possible to produce coatings as thick as about 100 ~, if desired The minimum size of the particles to be coated can be determined by sieve analysis, and the maximum size of the atomized droplets of coating fluid can be read from charts available from the manufacturer of the nozzle, when the viscosity of the fluid and the pressure is known.
In a preferred embodiment of the process according to the invention the water soluble or water dispersible particles to be coated contain one or more enzymes as an active ingredient, e.g. proteases, amylases, lipases or celluloses.
In another preferred embodiment of the process according to the invention the enzyme or enzymes are bacterial proteinases.
In another preferred embodiment of the process according to the invention the bacterial proteinases are precoated in order to reduce dust formation.
In another preferred embodiment of the process according to the invention the bacterial proteinases are ALCALASE P or ALCALASE M.
ALCALASE, which is a trade mark belonging to NOVO
INDUSTRI A/S, is a microbial proteinase. ALCALASE P is a prilled ALCALASE. ALCALASE M is ALCALASE which is treated by means of a Marumerizer as described in our British Patent No. 1,362,365, issued on December 4, 1974, and in our published French Patent No. 2,099,349.
In another preferred embodiment of the process according to the invention the enzyme or enzymes are bacterial or fungal carbohydrases.
_3_ In another preferred embodiment of the process according to the invention the bacterial amylases are thermally stable amylases manufactured according to sritish Patent No. 1,296,839.
In another preferred embodiment of the process according to the invention the macromolecular film forming, water soluble or water dispersible coating agent is a cellulose derivative.
In another preferred embodiment of the process according to the invention the cellulose derivative is methyl cellulose, hydroxybutylmethyl cellulose, sodium carboxymethyl cellulose, hydroxyethylmethyl cellulose or hydroxypropylmethyl cellulose.
In another preferred embodiment of the process according to the invention the macromolecular film forming, water soluble or water dispersible coating agent is a polyvinylpyrrolidone.
104g334 ~ n another preferred embodiment of the process according to the in~ention t~le macromolecular film forming, water soluble or water dispersable coating agent is a polyethylene glycol~
preferably of a molecular weight of between about 400 and about 6000.
In another preferred embodiment of the process according to the invention the macromolecular film formingJ water soluble or water dispersable coating agent is a methacrylic resin.
In another preferred embodiment of the process according to the invention the macromolecular film forming, water soluble or water dispersable coating agent is gelatine.
In another preferred embodiment of the process according to the invention the coating fluid contains a-plasticizer.
In another preferred embodiment of the`process according to the invention the plasticizer is a glycerol.
In another preferred embodiment of the process according to the invention the glycerol is used in an amount of up to 60 % of the dry weight of the coating agent, preferably in an amount of between 10 and ~0 % of the dry weight of the coating agent.
In another preferred embodiment of the process according to the invention the concentration of the macromolecular film forming, water soluble or water dispersable coating agent in the coating fluid is between 2 and 50 weight-%.
In another preferre'd embodiment of the process according to the invention the concentration of the macromolecular film forming, water soluble or water dispersable coating agent in the coating fluid is between 4 and 10 weight-%.
In another preferred embodiment of the process according to the invention the mean diameter of the particles to be coated is between 0.1 and o.6 mm.
In another preferred embodiment of the process according to the invention the mean diameter of the particles to be coated is between 0.2 and o.6 mm.
1~4~334 1ll anot~le~ p~eferred em'~o~imerlt of tile p~ocess according to the invention the thlckness o~ the coating layer is be~ween 0.1 and 10 ~.
In another preferred embodiment o~ the process-according to the invention ~he thickness of the coating layer is between 0.5 and 1 ~. -The process according to the invention can be carried outin a continuous manner as well as batchwise. However, in a pre-ferred embodiment of the invention the process is carried out batchwise. In all the following examples the process is~ carried out batchwise.
The invention also encompasses a coated product comprising coated water soluble or water dispersable particles, whenever prepared by means of the process according to the invention.
The water soluble or water dispersable particles can be of any material which, for any reason, is to be coated. Examples of materials encompassed are enzyme additives, e.g. proteolytic enzyme additives for detergents, medicaments in pellet form, e.g.
oral penicillin preparations or hygroscopic substances, e.g.
fertilizers.
Coating of the particles is carried out for various reasons, e.g. in order to minimize dust formation, to protect against ultra-violet radiation, humidity or acidity, to minimize contamination, and the like.
The coating agent can be any macromolecular film forming, water soluble or water dispersable coating agent, e.g.
METHOCEL ~ MC 15: methyl cellulose of a methoxyl DS (Degree of Substitution) of 1.64 to 1.92 and o~ a DP (Degree of Poly-merization) corresponding to viscosities from 8 cP to 10,000 cP
in a 2 % aqueous solution at 20C.
TYLOSE ~ C 10: sodium carboxymethyl cellulose of a DS from 0.4 to 1.5 and a DP from 50 to 1000.
_ . ' , 10~9334 TYLoS~ 20: methylhydroxyeth~l cellulose (or hydroxyethylmethyl cellulose) of a methoxyl DS from 1.0 to
2.0, a hydroxyethyl DS from 0.1 to 0.5 and a DP from 50 to 1000.
l~ETHOCEL ~ XD 1181: hydroxypropylmethyl cellulose of a methoxyl DS from 1.0 to 2.0, a hydroxypropyl DS from 0.1 to 0.5, and a DP from 50 to 1000.
KOLLIDON ~ K 25 PVP: polyvinylpyrrolidone of an average molecular weight of 10,000, 40,000, 160,000 and 360,000 and mixtures thereof resulting in any intermediate average molecular weight.
CAR~30WAX ~ : polyethylene glycols of average mole-cular weights of 400, 600, 1000, 1540, 4000, 6000 and mixtures thereof of any intermediate average molecular weight.
EUDRAGIT ~ E 30 D: methacrylic resins, aqueous dispersions thereof. rrhis tablet lacquer is completely in-soluble in alkaline liquids.
SOLUGEL ~ : gelatine.
Polypropylene glycols.
Polyvinyl alcohols.
Alginates.
The concentration of the coating agent in the aqueous or substantially aqueous solution or dispersion corresponds to a viscosity which is suitable for atomization. Usually, as mentioned before, the concentration is between 2 and 50 weight-%, preferably between 4 and 10 weight-%. The limits, however, are highly dependent on the individual coating agent used. The average diameter of the particles to be coated is usually between 100 ~ and 600 to 1000 ~, preferably between 200 ~ and 600 ~. The relative humidity of the outlet air should usually not exceed 60%. The temperature of the air, which is used to fluidize the particles to be coated, should be adjusted in con-sideration of the nature of the particles to be coated.
7 ~
A~ ..
~04~334 I
Th~ (lualit~ o'~ t~ oatir,cr, is not; in~luenced by the shape of the particles. F3y use of tile process of the invention it is possible to produce a perf~ct coating on splleres and on irregularly shaped particles as ~ell. Several of the known coating procedures are not well adapted to the coating of irregularly shaped particles which li are imperfectly coated, only. Therefore, the present process offers special advantages in connection with the coating of irregularly shaped particles. An example of such irregularly shaped particles is a prilled enzyme product includin~ prilled ALCALASE or ALCALASE P. When prilled ALCALASE is coated in accordance with the invention a product consisting of irregularly shaped particles having a-perfect coating is formed. Due to the irregular shape these particles have a very raduced tendency to segregate from the other particles of detergent compositions in powder form.
An additive consisting of spheroidal particles having a density different from the density of the particles of the other components of a powdery detergent composition will have a tendency to segregate from said other particles and thereby create an inhomogeneous detergent composition. The above irregularly shaped particles therefore offer special advantages.
According to the invention the coating fluid may contain a plasticizer such as triacetin, which is illustrated in the following example 2.
By using glycerol as a plasticizer in the coating fluid coated particles having specially advantageous dust levels can be obtained according to the invention.
By using glycerol as a plasticizer in the coating fluid in an amount of up to 60 per cent of the dry weight of the coating agent or up to the point when the coated particles are beginning to adhere to each other, preferably in an amount between 10 and ~0 per cent of the dry weight of the coating agent, the dust level of the coated particles is reduced significantly which will appear from the following.
~049334 rn o~de~ l;o ~i~e a bet~er ur)t1erstarl~ing of how to correla~e the different parameters of the process in order to obtain a relative humidity o~ the outlet air of less than 100~ the following calculation with reference to example 21 is presented. The inlet air, which was the air in the plant, had the following charac-teristics:
Temperature: 20C
Relative humidity: 50 ~ corresponding to 7 g of H20/kg air.
The rate of the coating fluidlwas 1700 ml/min. or 102 litre/hour. The coating fluid had a specific gravity of 1.0 g/cm~
and contained 10 % by weight of coating agent, corresponding to a water inlet amount from the coating fluid of 91.8 kg/hour.
The rate of fluidizing air was 8000 N m~/hour or 9600 kg of air/hour. Thus, the fluidizing air introduced 0.007 x 9600 =
67.2 kg of water in the systém per hour.
Thus, per hour a total of 91.8 + 67.2 kg of water was introduced into the system. This corresponds to~159.0 kg of water, which was removed from the system together with'about 9~00 kg of air. As the outlet air had a temperature of between 2~and 27C
this amount of humidity in the outlet air corresponds to a relative humidity in the outlet air of between 95 and 75 %. It is noted that this relative humidity is within the limit given for the relative humidity in claim 1.
In order to illustrate the invention the following examples are presented.
- Examples l to 10 illustrate the preparation of the coating fluid.
Example 1 Methyl cellulose (METHOCEL ~ MC 15) 50 g Deionized water 1000 g The methyl cellulose is triturated with about 33~ g of boiling water, after which the rest of the water (optionally cold) is added with s-ir~ing. The solutio~ is allowed to stand in a cold place.
- .
Exanple 2 Metilyl cellulose (ME~[~-IOCEL ~ MC 15) 50 g Deioni~ed water 1000 g Triacetin 5 g A solution of methyl cellulose and deionized water is pre-pared as described in Example 1, whereupon the triacetin is added.
Example 3 Sodium carboxymethyl cellulose (TYLOSE ~ C 10) 50 g Deionlzed water 1000 g The sodium carboxymethyl cellulose is dissolved in the water with stirringJ using a high speed mixer.
Example 4 Sodium carboxymethyl cellulose (TYLOSE ~ C 10) 100 g Deionized water 1000 g The sodium carboxymethyl cellulose is dissolved in the water with stirring~ using a high speed mixer.
Example 5 Methylhydroxyethyl cellulose ~YLOSE ~ MH 20) 50 g Deionized water lOpO g The methylhydroxyethyl cellulose is dissolved in the water with stirring, using a high speed mixér.
Example 6 Hydroxypropylmethyl cellulose (METHOCEL ~ XD 1181) 50 g Deionized water 1000 g The hydroxypropylmethyl cellulose is dissolved in the water with stirring, uslng a high speed mlxer.
Example 7 Gelatine (SOLUGEL ~ ) 50 g Deionized water 1000 g The gelatine is dissolved in the water with stirring, using a high speed mixer.
Example 8 Polyvinylpyrrolidone (KOLLIDON ~ K 25) 50 g Deionized water 1000 g The polyvinylpyrrolidone is dissolved in the water with stirring, using a high speed mixer.
Example 9 Polyethylene glycol (CARBOWAX ~ 4000) 50 g Deionized water 1000 g The polyethylene glycol is dissolved in the water with stirring, using a high speed mixer.
Example 10 Polyethylene glycol (CARBOWAX ~ 6000) 50 g Deionized water 1000 g The polyethylene glycol is dissolved in the water with stirring, using a high speed mixer.
The solutions prepared according to Examples 1 to 10 are used for the coating of prilled ALCALASE (ALCALASE P) in conventional and common fluid bed systems as stated in Examples 11 to 14 and 21.
Example 11 -Apparatus: "STREBA-l" (Aeromatic AG,Basel) ALCALASE P: 1000 g Nozzle ~.
- Pressure 2 1/2 ato .
Internal diameter 0.8 mm ~ .
Inlet temperature of -:
fluidizing air: 41-43C
: Temperature of parti-culate material: 31~-33C
; 30 Feed rate of coating fluid: 6 1/2 ml/min.
Fluidizing air: 8-10 scale units -.~. ' . ~ .
. ,; .i, ;
~ a !rl D ~
.__ Apparatus: "WS(i-5" (W. Glatt, Haltingen, Germany) ALCALASE P: 6000 g Mozzle Position of jacket: 0.5 Pressure 1 1/2 ato.
Internal diameter: 1.2 mm Inlet temperature of fluidizing air: -~2-45C
Temperature of O
particulate material: 31 -33 C
Feed rate of coating fluid: 35 ml/min.
Air velocity: 2 1/2 m/sec.
Example 13 . Apparatus: "WSG-30" (W. Glatt, Haltingen~
Germany) ALCALASE P:. ~5,000 g Nozzle - Position of jacket: 0.3 Pressure: 6 ato.
Internal diameter: 1.8 mm Inlet temperature of fluidizing air: ~2-45C .
Temperature of O 0 particulate material: 31 -33 C
Feed rate of coating fluid: 187 ml/min.
Fluidizing air: 5 scale units Example 14 Apparatus: "STREBA-60" (Aeromatic AG, Basel) ALCALASE P: 135 kg Nozzle Position of jacket: 1.0 Pressure: 6 ato.
Internal diameter: 2~ mm :i nlet te~ t,ure oP
fluidizing air: 42-l~5C
Temperat,ure of particulate material: 31-3~C
Feed rate of coating flu'id: 325 ml/min.
Rate Or fluidiæing air: corresponding to position 3 of damper.
In all cases particulate products are produced having remark-ably good properties.
The amount of coating layer on the ~articles and the amount of dust present in some of the coated products prepared according to Examples 12 to 14 appear from the following table II.
Table II
Coating fluid Amount of Amount of dust Example p~epared according coating layer on in ~g/100 g of prod~cr No. to Example No.coated product Total Enzyme 1 1 % 20 2.1 1 1 % 20 1.6 6 1 % , 5 o.8 12 1 1/2 ~ 20 2.6 % 1 5 1 . 8 1 1 1/2 % 20 0. 8 6 2 % 10 1.1
l~ETHOCEL ~ XD 1181: hydroxypropylmethyl cellulose of a methoxyl DS from 1.0 to 2.0, a hydroxypropyl DS from 0.1 to 0.5, and a DP from 50 to 1000.
KOLLIDON ~ K 25 PVP: polyvinylpyrrolidone of an average molecular weight of 10,000, 40,000, 160,000 and 360,000 and mixtures thereof resulting in any intermediate average molecular weight.
CAR~30WAX ~ : polyethylene glycols of average mole-cular weights of 400, 600, 1000, 1540, 4000, 6000 and mixtures thereof of any intermediate average molecular weight.
EUDRAGIT ~ E 30 D: methacrylic resins, aqueous dispersions thereof. rrhis tablet lacquer is completely in-soluble in alkaline liquids.
SOLUGEL ~ : gelatine.
Polypropylene glycols.
Polyvinyl alcohols.
Alginates.
The concentration of the coating agent in the aqueous or substantially aqueous solution or dispersion corresponds to a viscosity which is suitable for atomization. Usually, as mentioned before, the concentration is between 2 and 50 weight-%, preferably between 4 and 10 weight-%. The limits, however, are highly dependent on the individual coating agent used. The average diameter of the particles to be coated is usually between 100 ~ and 600 to 1000 ~, preferably between 200 ~ and 600 ~. The relative humidity of the outlet air should usually not exceed 60%. The temperature of the air, which is used to fluidize the particles to be coated, should be adjusted in con-sideration of the nature of the particles to be coated.
7 ~
A~ ..
~04~334 I
Th~ (lualit~ o'~ t~ oatir,cr, is not; in~luenced by the shape of the particles. F3y use of tile process of the invention it is possible to produce a perf~ct coating on splleres and on irregularly shaped particles as ~ell. Several of the known coating procedures are not well adapted to the coating of irregularly shaped particles which li are imperfectly coated, only. Therefore, the present process offers special advantages in connection with the coating of irregularly shaped particles. An example of such irregularly shaped particles is a prilled enzyme product includin~ prilled ALCALASE or ALCALASE P. When prilled ALCALASE is coated in accordance with the invention a product consisting of irregularly shaped particles having a-perfect coating is formed. Due to the irregular shape these particles have a very raduced tendency to segregate from the other particles of detergent compositions in powder form.
An additive consisting of spheroidal particles having a density different from the density of the particles of the other components of a powdery detergent composition will have a tendency to segregate from said other particles and thereby create an inhomogeneous detergent composition. The above irregularly shaped particles therefore offer special advantages.
According to the invention the coating fluid may contain a plasticizer such as triacetin, which is illustrated in the following example 2.
By using glycerol as a plasticizer in the coating fluid coated particles having specially advantageous dust levels can be obtained according to the invention.
By using glycerol as a plasticizer in the coating fluid in an amount of up to 60 per cent of the dry weight of the coating agent or up to the point when the coated particles are beginning to adhere to each other, preferably in an amount between 10 and ~0 per cent of the dry weight of the coating agent, the dust level of the coated particles is reduced significantly which will appear from the following.
~049334 rn o~de~ l;o ~i~e a bet~er ur)t1erstarl~ing of how to correla~e the different parameters of the process in order to obtain a relative humidity o~ the outlet air of less than 100~ the following calculation with reference to example 21 is presented. The inlet air, which was the air in the plant, had the following charac-teristics:
Temperature: 20C
Relative humidity: 50 ~ corresponding to 7 g of H20/kg air.
The rate of the coating fluidlwas 1700 ml/min. or 102 litre/hour. The coating fluid had a specific gravity of 1.0 g/cm~
and contained 10 % by weight of coating agent, corresponding to a water inlet amount from the coating fluid of 91.8 kg/hour.
The rate of fluidizing air was 8000 N m~/hour or 9600 kg of air/hour. Thus, the fluidizing air introduced 0.007 x 9600 =
67.2 kg of water in the systém per hour.
Thus, per hour a total of 91.8 + 67.2 kg of water was introduced into the system. This corresponds to~159.0 kg of water, which was removed from the system together with'about 9~00 kg of air. As the outlet air had a temperature of between 2~and 27C
this amount of humidity in the outlet air corresponds to a relative humidity in the outlet air of between 95 and 75 %. It is noted that this relative humidity is within the limit given for the relative humidity in claim 1.
In order to illustrate the invention the following examples are presented.
- Examples l to 10 illustrate the preparation of the coating fluid.
Example 1 Methyl cellulose (METHOCEL ~ MC 15) 50 g Deionized water 1000 g The methyl cellulose is triturated with about 33~ g of boiling water, after which the rest of the water (optionally cold) is added with s-ir~ing. The solutio~ is allowed to stand in a cold place.
- .
Exanple 2 Metilyl cellulose (ME~[~-IOCEL ~ MC 15) 50 g Deioni~ed water 1000 g Triacetin 5 g A solution of methyl cellulose and deionized water is pre-pared as described in Example 1, whereupon the triacetin is added.
Example 3 Sodium carboxymethyl cellulose (TYLOSE ~ C 10) 50 g Deionlzed water 1000 g The sodium carboxymethyl cellulose is dissolved in the water with stirringJ using a high speed mixer.
Example 4 Sodium carboxymethyl cellulose (TYLOSE ~ C 10) 100 g Deionized water 1000 g The sodium carboxymethyl cellulose is dissolved in the water with stirring~ using a high speed mixer.
Example 5 Methylhydroxyethyl cellulose ~YLOSE ~ MH 20) 50 g Deionized water lOpO g The methylhydroxyethyl cellulose is dissolved in the water with stirring, using a high speed mixér.
Example 6 Hydroxypropylmethyl cellulose (METHOCEL ~ XD 1181) 50 g Deionized water 1000 g The hydroxypropylmethyl cellulose is dissolved in the water with stirring, uslng a high speed mlxer.
Example 7 Gelatine (SOLUGEL ~ ) 50 g Deionized water 1000 g The gelatine is dissolved in the water with stirring, using a high speed mixer.
Example 8 Polyvinylpyrrolidone (KOLLIDON ~ K 25) 50 g Deionized water 1000 g The polyvinylpyrrolidone is dissolved in the water with stirring, using a high speed mixer.
Example 9 Polyethylene glycol (CARBOWAX ~ 4000) 50 g Deionized water 1000 g The polyethylene glycol is dissolved in the water with stirring, using a high speed mixer.
Example 10 Polyethylene glycol (CARBOWAX ~ 6000) 50 g Deionized water 1000 g The polyethylene glycol is dissolved in the water with stirring, using a high speed mixer.
The solutions prepared according to Examples 1 to 10 are used for the coating of prilled ALCALASE (ALCALASE P) in conventional and common fluid bed systems as stated in Examples 11 to 14 and 21.
Example 11 -Apparatus: "STREBA-l" (Aeromatic AG,Basel) ALCALASE P: 1000 g Nozzle ~.
- Pressure 2 1/2 ato .
Internal diameter 0.8 mm ~ .
Inlet temperature of -:
fluidizing air: 41-43C
: Temperature of parti-culate material: 31~-33C
; 30 Feed rate of coating fluid: 6 1/2 ml/min.
Fluidizing air: 8-10 scale units -.~. ' . ~ .
. ,; .i, ;
~ a !rl D ~
.__ Apparatus: "WS(i-5" (W. Glatt, Haltingen, Germany) ALCALASE P: 6000 g Mozzle Position of jacket: 0.5 Pressure 1 1/2 ato.
Internal diameter: 1.2 mm Inlet temperature of fluidizing air: -~2-45C
Temperature of O
particulate material: 31 -33 C
Feed rate of coating fluid: 35 ml/min.
Air velocity: 2 1/2 m/sec.
Example 13 . Apparatus: "WSG-30" (W. Glatt, Haltingen~
Germany) ALCALASE P:. ~5,000 g Nozzle - Position of jacket: 0.3 Pressure: 6 ato.
Internal diameter: 1.8 mm Inlet temperature of fluidizing air: ~2-45C .
Temperature of O 0 particulate material: 31 -33 C
Feed rate of coating fluid: 187 ml/min.
Fluidizing air: 5 scale units Example 14 Apparatus: "STREBA-60" (Aeromatic AG, Basel) ALCALASE P: 135 kg Nozzle Position of jacket: 1.0 Pressure: 6 ato.
Internal diameter: 2~ mm :i nlet te~ t,ure oP
fluidizing air: 42-l~5C
Temperat,ure of particulate material: 31-3~C
Feed rate of coating flu'id: 325 ml/min.
Rate Or fluidiæing air: corresponding to position 3 of damper.
In all cases particulate products are produced having remark-ably good properties.
The amount of coating layer on the ~articles and the amount of dust present in some of the coated products prepared according to Examples 12 to 14 appear from the following table II.
Table II
Coating fluid Amount of Amount of dust Example p~epared according coating layer on in ~g/100 g of prod~cr No. to Example No.coated product Total Enzyme 1 1 % 20 2.1 1 1 % 20 1.6 6 1 % , 5 o.8 12 1 1/2 ~ 20 2.6 % 1 5 1 . 8 1 1 1/2 % 20 0. 8 6 2 % 10 1.1
3 % lo o.8 . -. .. _.
1 % 5 ~ 1.8 1 1/2 % 20 1.0 3 1 1 % 5 l.o 1 % lo 1.6 14 1 1/2 % 5o ~.4 1 1 % 15 1.6 Examples 15 to 20 illustrate the preparation of a coating fluid containing glycerol and corresponding coating fluids without glycerol.
.
' ' ' .
`'~' ' 1~49334 ~`xa.~t~
Methyl cell~llose (M~ HOCEL ~ MC 15) 50 g Deioni,zed water 950 g The methyl cellulose is triturated with about 33~ g Or boiling water, after which the rest Or the water (optionally cold) is added with stirring. The solution is allowed to stand in a cold place.
Example 16 Methyl cellulose (METHOCEL ~ MC 15) 42.5 g Glycerol 7,5 g Deionized water 950.0 g A solution of methyl cellulose and deionized water is prepared as described in Example 15, whereupon the glycerol is added.
Example 17 Sodium carboxymethyl cellulose (CELLOFAS ~ B 5) 100 g Deionized water 900 g The sodium carboxymethyl cellulose is triturated with about 3~3 g of boiling water, after which the rest of the water (optionally cold) is added with stirring. The solution is allowed to stand in a cold place.
Example 18 Sodium carboxymethyl cellulose (CELLOFAS ~ B 5) 85 g Glycerol ~ 15-g Deionized water 900 g A solution of sodium carboxymethyl cellulose and deionized water is prepared as described in Example 17, whereupon the glycerol is added.
Example 19 Sodium carboxymethyl cellulose (CEKOL ~ HS) 10,0 g Deionized water 900 g A solution af sodium carboxymethyl cellulose and deionized water is prepared as described in Example 17.
, -14-. .
.
.. .... . . .
~049334 E~ample 20 Sodium carbox~methyl cellulose (CEKOL ~ HS) 85 g Glycerol 15 g Deionized water goo g A solution of sodium carboxymethyl cellulose and deionized water is prepared as described in Example 17, whereupon the glycerol is added.
The solutions prepared according to Examples 15 to 20 are used for the co~ting o~ ALCALASE M in a fluid bed system as stated in Example 21 Example 21 Apparatus: "WSG-300" (W. Glatt, Haltingen, Gerrr~any) ALCALASE M: 600 kg Nozzle six-headed nozzle Internal diameter: 1.2 mm -~
Jacket diameter: 6.o mm Pressure: 6.o ato.
Inlet temperature of fluidizing air: 46-50C
Temperature of particulate material: 23-27C
Feed rate of coating fluid: 1700 ml/min.
Fluidizing air: 8000 N m3/hour In all cases particulate products are produced having rernark-ably good properties, especially in regard to the dust level.
The amount Or dust present in the coated products prepared according to Example 21 appears from the following table III.
. ' '. ' 109~334 'ilat~Le-:r~:r Coating ~ id Amount of Amount of dust Example prepared accordil~K coating layer on in ug/100 g of~Eroduct No. to E~'xarnple No. coated product Total Enzvme . _ _ _ _ _Y
. 1 % 20 1.2 16 1 % 10 0.5 21 17 1 ~ 15 1.6 1~ 1 % 10 0.7 19 1 ~ 30 1.~
1 ~ 10 0.8 . . _ It appears from the above table III ~hat by using glycerol as a plasticizer in the coating fluid a remarka'~ly advantageous effect on the dust level of the coated particles is obtained.
.
.
1 % 5 ~ 1.8 1 1/2 % 20 1.0 3 1 1 % 5 l.o 1 % lo 1.6 14 1 1/2 % 5o ~.4 1 1 % 15 1.6 Examples 15 to 20 illustrate the preparation of a coating fluid containing glycerol and corresponding coating fluids without glycerol.
.
' ' ' .
`'~' ' 1~49334 ~`xa.~t~
Methyl cell~llose (M~ HOCEL ~ MC 15) 50 g Deioni,zed water 950 g The methyl cellulose is triturated with about 33~ g Or boiling water, after which the rest Or the water (optionally cold) is added with stirring. The solution is allowed to stand in a cold place.
Example 16 Methyl cellulose (METHOCEL ~ MC 15) 42.5 g Glycerol 7,5 g Deionized water 950.0 g A solution of methyl cellulose and deionized water is prepared as described in Example 15, whereupon the glycerol is added.
Example 17 Sodium carboxymethyl cellulose (CELLOFAS ~ B 5) 100 g Deionized water 900 g The sodium carboxymethyl cellulose is triturated with about 3~3 g of boiling water, after which the rest of the water (optionally cold) is added with stirring. The solution is allowed to stand in a cold place.
Example 18 Sodium carboxymethyl cellulose (CELLOFAS ~ B 5) 85 g Glycerol ~ 15-g Deionized water 900 g A solution of sodium carboxymethyl cellulose and deionized water is prepared as described in Example 17, whereupon the glycerol is added.
Example 19 Sodium carboxymethyl cellulose (CEKOL ~ HS) 10,0 g Deionized water 900 g A solution af sodium carboxymethyl cellulose and deionized water is prepared as described in Example 17.
, -14-. .
.
.. .... . . .
~049334 E~ample 20 Sodium carbox~methyl cellulose (CEKOL ~ HS) 85 g Glycerol 15 g Deionized water goo g A solution of sodium carboxymethyl cellulose and deionized water is prepared as described in Example 17, whereupon the glycerol is added.
The solutions prepared according to Examples 15 to 20 are used for the co~ting o~ ALCALASE M in a fluid bed system as stated in Example 21 Example 21 Apparatus: "WSG-300" (W. Glatt, Haltingen, Gerrr~any) ALCALASE M: 600 kg Nozzle six-headed nozzle Internal diameter: 1.2 mm -~
Jacket diameter: 6.o mm Pressure: 6.o ato.
Inlet temperature of fluidizing air: 46-50C
Temperature of particulate material: 23-27C
Feed rate of coating fluid: 1700 ml/min.
Fluidizing air: 8000 N m3/hour In all cases particulate products are produced having rernark-ably good properties, especially in regard to the dust level.
The amount Or dust present in the coated products prepared according to Example 21 appears from the following table III.
. ' '. ' 109~334 'ilat~Le-:r~:r Coating ~ id Amount of Amount of dust Example prepared accordil~K coating layer on in ug/100 g of~Eroduct No. to E~'xarnple No. coated product Total Enzvme . _ _ _ _ _Y
. 1 % 20 1.2 16 1 % 10 0.5 21 17 1 ~ 15 1.6 1~ 1 % 10 0.7 19 1 ~ 30 1.~
1 ~ 10 0.8 . . _ It appears from the above table III ~hat by using glycerol as a plasticizer in the coating fluid a remarka'~ly advantageous effect on the dust level of the coated particles is obtained.
.
.
Claims (23)
1. A process for coating water soluble or water dispersible particles by means of the fluid bed technique, which comprises introducing the particles to be coated in a fluid bed reactor, the mean diameter of the particles to be coated being in the range of from 0.1 to 0.6 mm, and introducing a coating fluid essentially consisting of an aqueous or substantially aqueous solution or dispersion of a macromolecular film forming, water soluble or water dispersible coating agent by means of atomi-zation, wherein the relative humidity of the outlet air from the fluid bed reactor is below 100% and wherein the maximum size of the atomized droplets of the coating fluid does not exceed the minimum size of the particles to be coated.
2. A process as claimed in claim 1, wherein the water soluble or water dispersible particles to be coated contain as an active ingredient one or more enzymes.
3. A process as claimed in claim 2, wherein the enzyme is bacterial proteinase.
4. A process as claimed in claim 3, wherein the bacterial proteinase is precoated in order to reduce dust formation.
5. A process as claimed in claim 4, wherein the bacterial proteinase is microbial proteinase.
6. A process as claimed in claim 3, wherein the bacterial proteinase is alkaline resistant proteinase.
7. A process as claimed in claim 2, wherein the enzyme or is bacterial or fungal carbohydrase.
8. A process as claimed in claim 7, wherein the bacterial amylase is thermally stable amylases.
9. A process as claimed in claim 1, wherein the macromolecular film forming, water soluble or water dispersible coating agent is a cellulose derivative.
10. A process as claimed in claim 9, wherein the cellulose derivative is methyl cellulose, hydroxybutylmethyl cellulose, sodium carboxymethyl cellulose, hydroxyethylmethyl cellulose or hydroxypropylmethyl cellulose.
11. A process as claimed in claims 1, 2 or 3, wherein the macromolecular film forming, water soluble or water dispersible coating agent is a polyvinylpyrrolidone.
12. A process as claimed in claims 1, 2 or 3, wherein the macromolecular film forming, water soluble or water dispersible coating agent is a polyethylene glycol, preferably of a molecular weight of between about 400 and about 6000.
13. A process as claimed in claims 1, 2 or 3, wherein the macromolecular film forming, water soluble or water dispersible coating agent is a methacrylic resin.
14. A process as claimed in claims 1, 2 or 3, wherein the macromolecular film forming, water soluble or water dispersible coating agent is a gelatine.
15. A process as claimed in claim 1, wherein the coating fluid contains a plasticizer.
16. A process as claimed in claim 15, wherein the plastici-zer is glycerol.
17. A process as claimed in claim 16, wherein the glycerol is used in an amount of up to 60% of the dry weight of the coat-ing agent, preferably in an amount between 10 and 30% of the dry weight of the coating agent.
18. A process as claimed in claim 9, wherein the concentration of the macromolecular film forming, water soluble or water dispersible coating agent in the coating fluid is between 2 and 50 weight-%.
19. A process as claimed in claim 18, wherein the concentration of the macromolecular film forming, water soluble or water dispersible coating agent in the coating fluid is between 4 and 10 weight-%.
20. A process as claimed in claim 1, in which the mean diameter of the particles to be coated is between 0.2 and 0.6 mm.
21. A process as claimed in claim 1, in which the thick-ness of the coating layer is between 0.1 and 10 µ.
22. A process as claimed in claim 21, in which the thick-ness of the coating layer is between 0.5 and 1 µ.
23. A process as claimed in claims 1, 2 or 3, in which the coating operation is performed batchwise.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB34993/73A GB1483591A (en) | 1973-07-23 | 1973-07-23 | Process for coating water soluble or water dispersible particles by means of the fluid bed technique |
GB1084274 | 1974-03-11 |
Publications (1)
Publication Number | Publication Date |
---|---|
CA1049334A true CA1049334A (en) | 1979-02-27 |
Family
ID=26247797
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CA205,367A Expired CA1049334A (en) | 1973-07-23 | 1974-07-22 | Process for coating water soluble or water dispersible particles by means of the fluid bed technique |
Country Status (16)
Country | Link |
---|---|
JP (1) | JPS5071583A (en) |
AT (1) | AT357979B (en) |
AU (1) | AU498649B2 (en) |
BE (1) | BE817930A (en) |
CA (1) | CA1049334A (en) |
CH (1) | CH604923A5 (en) |
DE (1) | DE2435008A1 (en) |
DK (1) | DK384574A (en) |
ES (1) | ES428475A1 (en) |
FI (1) | FI219474A (en) |
FR (1) | FR2238530B1 (en) |
GB (1) | GB1483591A (en) |
IE (1) | IE41403B1 (en) |
IT (1) | IT1016947B (en) |
NL (1) | NL7409683A (en) |
SE (1) | SE7409471L (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4828882A (en) * | 1987-03-16 | 1989-05-09 | Canadian Patents & Developments Limited | Particle encapsulation technique |
US5211985A (en) * | 1991-10-09 | 1993-05-18 | Ici Canada, Inc. | Multi-stage process for continuous coating of fertilizer particles |
Families Citing this family (390)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS587497A (en) * | 1981-07-06 | 1983-01-17 | ダスキンフランチヤイズ株式会社 | Bleaching agent composition |
JPS60189548U (en) * | 1984-05-24 | 1985-12-16 | 昭和電工株式会社 | Detergent capsule with enzyme capsule |
US4689297A (en) * | 1985-03-05 | 1987-08-25 | Miles Laboratories, Inc. | Dust free particulate enzyme formulation |
EP0270608B1 (en) * | 1986-05-21 | 1990-08-22 | Novo Nordisk A/S | Coated detergent enzymes |
US4759956A (en) * | 1987-05-22 | 1988-07-26 | Lever Brothers Company | Process for encapsulating particles using polymer latex |
JP2815925B2 (en) * | 1989-09-26 | 1998-10-27 | 花王株式会社 | Method for coating particles for detergent formulation |
US5254283A (en) * | 1991-01-17 | 1993-10-19 | Genencor International, Inc. | Isophthalic polymer coated particles |
DE69534513T2 (en) | 1994-03-08 | 2006-07-27 | Novozymes A/S | NOVEL ALKALINE CELLULASES |
US5824531A (en) | 1994-03-29 | 1998-10-20 | Novid Nordisk | Alkaline bacilus amylase |
AR000862A1 (en) | 1995-02-03 | 1997-08-06 | Novozymes As | VARIANTS OF A MOTHER-AMYLASE, A METHOD TO PRODUCE THE SAME, A DNA STRUCTURE AND A VECTOR OF EXPRESSION, A CELL TRANSFORMED BY SUCH A DNA STRUCTURE AND VECTOR, A DETERGENT ADDITIVE, DETERGENT COMPOSITION, A COMPOSITION FOR AND A COMPOSITION FOR THE ELIMINATION OF |
CN102080070B (en) | 1995-03-17 | 2016-01-20 | 诺沃奇梅兹有限公司 | new endoglucanase |
CA2270593C (en) | 1996-11-04 | 2005-06-07 | Novo Nordisk A/S | Subtilase variants and compositions |
KR100591553B1 (en) | 1996-11-04 | 2006-06-19 | 노보자임스 에이/에스 | Subtilase variants and composition |
ATE441704T1 (en) | 1998-11-27 | 2009-09-15 | Novozymes As | VARIANTS OF A LIPOLYTIC ENZYME |
EP1803817B1 (en) | 1998-12-18 | 2011-04-06 | Novozymes A/S | Subtilase enzymes of the I-S1 and I-S2 sub-groups having an additional amino acid residue in an active site loop region |
PL343506A1 (en) | 1999-02-10 | 2001-08-27 | Dsm Nv | Granulates containing feed-enzymes |
WO2000060058A2 (en) | 1999-03-31 | 2000-10-12 | Novozymes A/S | Polypeptides having alkaline alpha-amylase activity and nucleic acids encoding same |
JP4745503B2 (en) | 1999-03-31 | 2011-08-10 | ノボザイムス アクティーゼルスカブ | Polypeptides having alkaline α-amylase activity and nucleic acids encoding them |
DE60040282D1 (en) | 1999-05-20 | 2008-10-30 | Novozymes As | SUBTILASE ENZYMES OF I-S1 AND I-S2 SUB-GROUPS WITH AT LEAST ONE ADDITIONAL AMINO ACID BETWEEN POSITIONS 132 AND 133 |
ATE407201T1 (en) | 1999-05-20 | 2008-09-15 | Novozymes As | SUBTILASE ENZYMES OF THE I-S1 AND I-S2 SUBGROUPS WITH AT LEAST ONE ADDITIONAL AMINO ACID RESIDUE BETWEEN POSITIONS 126 AND 127 |
AU4392900A (en) | 1999-05-20 | 2000-12-12 | Novozymes A/S | Subtilase enzymes of the i-s1 and i-s2 sub-groups having at least one additionalamino acid residue between positions 127 and 128 |
AU4393100A (en) | 1999-05-20 | 2000-12-12 | Novozymes A/S | Subtilase enzymes of the i-s1 and i-s2 sub-groups having at least one additionalamino acid residue between positions 125 and 126 |
DE60040284D1 (en) | 1999-05-20 | 2008-10-30 | Novozymes As | SUBTILASE ENZYMES OF I-S1 AND I-S2 SUB-GROUPS WITH AT LEAST ONE ADDITIONAL AMINO ACID BETWEEN POSITIONS 129 AND 130 |
EP1183342B2 (en) | 1999-05-20 | 2012-06-13 | Novozymes A/S | Subtilase enzymes of the i-s1 and i-s2 sub-groups having at least one additional amino acid residue between positions 128 and 129 |
DE19929257A1 (en) | 1999-06-25 | 2000-12-28 | Basf Ag | Production of polymer-coated granulated animal feed additive, useful in production of pelletized animal feed, involves granulating mixture of carrier and enzyme and coating with suitable organic polymer |
EP2206786A1 (en) | 1999-08-31 | 2010-07-14 | Novozymes A/S | Novel proteases and variants thereof |
US6924133B1 (en) * | 1999-10-01 | 2005-08-02 | Novozymes A/S | Spray dried enzyme product |
JP3610431B2 (en) * | 2000-07-17 | 2005-01-12 | マークテック株式会社 | Magnetic powder compound for wet magnetic particle testing |
AU2001279614B2 (en) | 2000-08-21 | 2006-08-17 | Novozymes A/S | Subtilase enzymes |
AU2002210379A1 (en) | 2000-10-13 | 2002-04-22 | Novozymes A/S | Subtilase variants |
US20040091994A1 (en) | 2000-10-13 | 2004-05-13 | Carsten Andersen | Alpha-amylase variant with altered properties |
EP2159279A3 (en) | 2001-05-15 | 2010-05-12 | Novozymes A/S | Alpha-amylase variant with altered properties |
DK1414956T3 (en) | 2001-06-22 | 2008-03-03 | Genencor Int | Highly impact resistant granules |
WO2003000941A2 (en) | 2001-06-26 | 2003-01-03 | Novozymes A/S | Polypeptides having cellobiohydrolase i activity and polynucleotides encoding same |
DK200101090A (en) | 2001-07-12 | 2001-08-16 | Novozymes As | Subtilase variants |
US7501269B2 (en) | 2002-01-15 | 2009-03-10 | Basf Aktiengesellschaft | Granulates containing feed-enzymes |
ATE494368T1 (en) | 2002-10-01 | 2011-01-15 | Novozymes As | POLYPEPTIDES OF THE GH-61 FAMILY |
TWI319007B (en) | 2002-11-06 | 2010-01-01 | Novozymes As | Subtilase variants |
CN1738899A (en) | 2002-12-11 | 2006-02-22 | 诺和酶股份有限公司 | Detergent composition |
US7348168B2 (en) | 2002-12-20 | 2008-03-25 | Novozymes A/S | Polypeptides having cellobiohydrolase II activity and polynucleotides encoding same |
WO2004058933A1 (en) * | 2002-12-24 | 2004-07-15 | Genencor International, Inc. | Mechanically robust plasticized granules |
EP1622921B1 (en) | 2003-05-02 | 2010-06-16 | Novozymes Inc. | Variants of beta-glucosidases |
WO2004101760A2 (en) | 2003-05-12 | 2004-11-25 | Genencor International, Inc. | Novel lipolytic enzyme elip |
EP1625202A4 (en) | 2003-05-12 | 2010-10-20 | Genencor Int | Novel lipolytic enzyme lip1 |
WO2004101759A2 (en) | 2003-05-12 | 2004-11-25 | Genencor International, Inc. | Novel lipolytic enzyme lip2 |
EP1639106B1 (en) | 2003-06-19 | 2010-05-26 | Novozymes A/S | Proteases |
AU2004252572B2 (en) | 2003-06-25 | 2011-09-08 | Novozymes A/S | Polypeptides having alpha-amylase activity and polypeptides encoding same |
ES2424346T3 (en) | 2003-08-25 | 2013-10-01 | Novozymes Inc. | Variants of glycoside hydrolases |
BRPI0414959A (en) | 2003-10-10 | 2006-11-07 | Novozymes As | precursor protease variant, isolated nucleic acid sequence, recombinant nucleic acid construct, expression vector, and host cell, methods for producing the protease variant, for enhancing the nutritional value of an animal feed, and for treating proteins, a transgenic plant , or part of plant, transgenic, non-human animal, or products, or elements thereof, animal feed additive and composition, use of protease variant and / or composition, protease, and, 3d structure |
ATE516347T1 (en) | 2003-10-23 | 2011-07-15 | Novozymes As | PROTEASE WITH IMPROVED STABILITY IN DETERGENTS |
DK1682656T3 (en) | 2003-10-28 | 2013-11-18 | Novozymes Inc | Polypeptides with beta-glucosidase activity and polynucleotides encoding them |
EP1709165B1 (en) | 2004-01-06 | 2014-04-23 | Novozymes A/S | Polypeptides of alicyclobacillus |
US7361495B2 (en) | 2004-01-30 | 2008-04-22 | Novozymes, Inc. | Polypeptide from a cellulolytic fungus having cellulolytic enhancing activity |
JP2007521823A (en) | 2004-02-13 | 2007-08-09 | ノボザイムス アクティーゼルスカブ | Protease variant |
US7148404B2 (en) | 2004-05-04 | 2006-12-12 | Novozymes A/S | Antimicrobial polypeptides |
JP5623691B2 (en) | 2004-06-21 | 2014-11-12 | ノボザイムスアクティーゼルスカブ | Protease |
CA2854912A1 (en) | 2004-07-05 | 2006-01-12 | Novozymes A/S | Alpha-amylase variants with altered properties |
WO2006032277A1 (en) | 2004-09-21 | 2006-03-30 | Novozymes A/S | Subtilases |
US7811979B2 (en) | 2004-09-21 | 2010-10-12 | Novozymes A/S | Subtilases |
WO2006032278A1 (en) | 2004-09-21 | 2006-03-30 | Novozymes A/S | Subtilases |
EP1799819B1 (en) | 2004-09-30 | 2011-03-23 | Novozymes Inc. | Polypeptides having lipase activity and polynucleotides encoding same |
ATE447013T1 (en) | 2005-04-27 | 2009-11-15 | Novozymes Inc | POLYPEPTIDES WITH ENDOGLUCANASE ACTIVITY AND POLYNUCLEOTIDES CODING THEREFOR |
MX2007016045A (en) | 2005-07-08 | 2008-03-10 | Novozymes As | Subtilase variants. |
US8119387B2 (en) | 2005-08-16 | 2012-02-21 | Novozymes A/S | Polypeptides of strain Bacillus sp. P203 |
ATE530642T1 (en) | 2005-08-16 | 2011-11-15 | Novozymes As | SUBTILATE |
EP1941023B1 (en) | 2005-09-30 | 2017-04-05 | Novozymes Inc. | Methods for enhancing the degradation or conversion of cellulosic material |
EP1998793A1 (en) | 2006-03-22 | 2008-12-10 | Novozymes A/S | Use of polypeptides having antimicrobial activity |
ES2538360T3 (en) | 2006-07-21 | 2015-06-19 | Novozymes, Inc. | Methods to increase the secretion of polypeptides that have biological activity |
KR20090101193A (en) | 2006-12-21 | 2009-09-24 | 다니스코 유에스 인크. | Compositions and uses for an alpha-amylase polypeptide of bacillus species 195 |
MX2009009378A (en) | 2007-03-09 | 2009-09-22 | Danisco Us Inc Genencor Div | Alkaliphilic bacillus species a-amylase variants, compositions comprising a-amylase variants, and methods of use. |
DE102007016139A1 (en) | 2007-03-30 | 2008-10-02 | Jenabios Gmbh | Method for regioselective oxygenation of N-heterocycles |
JP2011505121A (en) | 2007-11-05 | 2011-02-24 | ダニスコ・ユーエス・インク | Alpha-amylase with modified properties |
BRPI0820500A2 (en) | 2007-11-05 | 2015-06-16 | Danisco Us Inc | Bacillus sp. Alpha-amylase variants Ts-23 with changed properties |
KR20100109945A (en) | 2008-02-04 | 2010-10-11 | 다니스코 유에스 인크. | Ts23 alpha-amylase variants with altered properties |
WO2009149283A1 (en) | 2008-06-06 | 2009-12-10 | Danisco Us Inc. | Saccharification enzyme composition |
US9040278B2 (en) | 2008-06-06 | 2015-05-26 | Danisco Us Inc. | Production of glucose from starch using alpha-amylases from Bacillus subtilis |
DK2447361T3 (en) | 2008-06-06 | 2015-01-05 | Danisco Us Inc | Alpha-amylase (AMYS) variants of Geobacillus stearothermophilus with improved properties |
US8323945B2 (en) | 2008-06-06 | 2012-12-04 | Danisco Us Inc. | Variant alpha-amylases from Bacillus subtilis and methods of uses, thereof |
DK2337837T4 (en) | 2008-09-25 | 2017-02-06 | Danisco Us Inc | ALPHA-AMYLASE MIXTURES AND PROCEDURES FOR USING IT |
EP2358878B1 (en) | 2008-11-20 | 2014-10-15 | Novozymes Inc. | Polypeptides having amylolytic enhancing activity and polynucleotides encoding same |
EP2373788A1 (en) | 2008-12-04 | 2011-10-12 | Novozymes Inc. | Polypeptides having cellulolytic enhancing activity and polynucleotides encoding same |
EP2376527A1 (en) | 2008-12-12 | 2011-10-19 | Novozymes Inc. | Polypeptides having lipase activity and polynucleotides encoding same |
ES2362460T3 (en) | 2008-12-23 | 2011-07-05 | Basf Se | MIXED CRYSTALS, PROCEDURE FOR OBTAINING AND USE IN THE MANUFACTURE OF BAKERY PRODUCTS. |
CN102341495A (en) | 2009-03-10 | 2012-02-01 | 丹尼斯科美国公司 | ALPHA-AMYLASES ASSOCIATED with BACILLUS MEGATERIUM DSM90, and method for using same |
BRPI1010238A2 (en) | 2009-04-01 | 2015-08-25 | Danisco Us Inc | Compositions and methods comprising alpha-amylase variants with altered properties |
EP2417254B1 (en) | 2009-04-08 | 2014-05-21 | Danisco US Inc. | Halomonas strain wdg195-related alpha-amylases, and methods of use, thereof |
CN102770534B (en) | 2009-09-17 | 2016-07-06 | 诺维信股份有限公司 | There is the polypeptide of cellulolytic enhancing activity and encode its polynucleotide |
MX2012003387A (en) | 2009-09-25 | 2012-04-10 | Novozymes As | Use of protease variants. |
MX339581B (en) | 2009-09-25 | 2016-06-01 | Novozymes As | Subtilase variants. |
US8148103B2 (en) | 2009-09-29 | 2012-04-03 | Novozymes, Inc. | Polypeptides having cellulolytic enhancing activity and polynucleotides encoding same |
US8586827B2 (en) | 2009-09-30 | 2013-11-19 | Novozymes, Inc. | Polypeptides having cellulolytic enhancing activity and polynucleotides encoding same |
CA2775244A1 (en) | 2009-09-30 | 2011-04-07 | Novozymes A/S | Polypeptides having cellulolytic enhancing activity and polynucleotides encoding same |
WO2011049945A2 (en) | 2009-10-23 | 2011-04-28 | Danisco Us Inc. | Methods for reducing blue saccharide |
WO2011076897A1 (en) | 2009-12-22 | 2011-06-30 | Novozymes A/S | Use of amylase variants at low temperature |
CN102918149A (en) | 2010-01-04 | 2013-02-06 | 诺维信公司 | Alpha-amylases |
CA2785624A1 (en) | 2010-01-22 | 2011-07-28 | Dupont Nutrition Biosciences Aps | Methods for producing amino-substituted glycolipid compounds |
MX369096B (en) | 2010-02-10 | 2019-10-29 | Novozymes As | Variants and compositions comprising variants with high stability in presence of a chelating agent. |
EP2357220A1 (en) | 2010-02-10 | 2011-08-17 | The Procter & Gamble Company | Cleaning composition comprising amylase variants with high stability in the presence of a chelating agent |
US8815559B2 (en) | 2010-02-18 | 2014-08-26 | Danisco Us Inc. | Amylase from nesterenkonia and methods of use, thereof |
DK2622070T3 (en) | 2010-09-30 | 2016-11-21 | Novozymes Inc | Variants of polypeptides having cellulolytic enhancing ACTIVITY AND POLYNUCLEOTIDES ENCODING THEM |
MX2013003236A (en) | 2010-09-30 | 2013-05-30 | Novozymes Inc | Variants of polypeptides having cellulolytic enhancing activity and polynucleotides encoding same. |
DK2640833T3 (en) | 2010-11-18 | 2016-11-28 | Novozymes Inc | Chimeric polypeptides having cellulolytic enhancing ACTIVITY AND POLYNUCLEOTIDES ENCODING THEM |
MX2013009178A (en) | 2011-02-16 | 2013-08-29 | Novozymes As | Detergent compositions comprising metalloproteases. |
JP2014511409A (en) | 2011-02-16 | 2014-05-15 | ノボザイムス アクティーゼルスカブ | Detergent composition containing metalloprotease |
WO2012110564A1 (en) | 2011-02-16 | 2012-08-23 | Novozymes A/S | Detergent compositions comprising m7 or m35 metalloproteases |
WO2012113340A1 (en) | 2011-02-23 | 2012-08-30 | Novozymes Inc. | Polypeptides having cellulolytic enhancing activity and polynucleotides encoding same |
WO2012135659A2 (en) | 2011-03-31 | 2012-10-04 | Novozymes A/S | Methods for enhancing the degradation or conversion of cellulosic material |
KR20140024365A (en) | 2011-04-08 | 2014-02-28 | 다니스코 유에스 인크. | Compositions |
MX2013011827A (en) | 2011-04-29 | 2014-01-08 | Novozymes Inc | Methods for enhancing the degradation or conversion of cellulosic material. |
US20140206594A1 (en) | 2011-06-24 | 2014-07-24 | Martin Simon Borchert | Polypeptides Having Protease Activity and Polynucleotides Encoding Same |
EP2540824A1 (en) | 2011-06-30 | 2013-01-02 | The Procter & Gamble Company | Cleaning compositions comprising amylase variants reference to a sequence listing |
IN2014CN00597A (en) | 2011-06-30 | 2015-04-03 | Novozymes As | |
EP2551335A1 (en) | 2011-07-25 | 2013-01-30 | The Procter & Gamble Company | Enzyme stabilized liquid detergent composition |
CN103748219A (en) | 2011-08-15 | 2014-04-23 | 诺维信公司 | Polypeptides having cellulase activity and polynucleotides encoding same |
CN103764822B (en) | 2011-08-19 | 2016-11-23 | 诺维信公司 | There is the polypeptide of proteinase activity |
MX350391B (en) | 2011-09-22 | 2017-09-06 | Novozymes As | Polypeptides having protease activity and polynucleotides encoding same. |
HUE039835T2 (en) | 2011-10-17 | 2019-02-28 | Novozymes As | Alpha-amylase variants and polynucleotides encoding same |
WO2013057143A2 (en) | 2011-10-17 | 2013-04-25 | Novozymes A/S | Alpha-amylase variants and polynucleotides encoding same |
RU2014121491A (en) | 2011-10-28 | 2015-12-10 | ДАНИСКО ЮЭс ИНК. | OPTIONS OF THE OPTIONAL ALPHA-AMILASE FORMING MALTHOXESOSE |
CA2855451A1 (en) | 2011-11-21 | 2013-08-15 | Novozymes, Inc. | Gh61 polypeptide variants and polynucleotides encoding same |
ES2631605T3 (en) | 2011-11-25 | 2017-09-01 | Novozymes A/S | Polypeptides with lysozyme activity and polynucleotides encoding them |
JP2015500006A (en) | 2011-11-25 | 2015-01-05 | ノボザイムス アクティーゼルスカブ | Subtilase variant and polynucleotide encoding the same |
WO2013087027A1 (en) | 2011-12-16 | 2013-06-20 | Novozymes, Inc. | Polypeptides having laccase activity and polynucleotides encoding same |
EP2607468A1 (en) | 2011-12-20 | 2013-06-26 | Henkel AG & Co. KGaA | Detergent compositions comprising subtilase variants |
US20140335596A1 (en) | 2011-12-20 | 2014-11-13 | Novozymes A/S | Subtilase Variants and Polynucleotides Encoding Same |
IN2014DN03298A (en) | 2011-12-22 | 2015-06-26 | Danisco Us Inc | |
CN104024407A (en) | 2011-12-22 | 2014-09-03 | 丹尼斯科美国公司 | Compositions and methods comprising lipolytic enzyme variant |
EP2798062B1 (en) | 2011-12-28 | 2018-02-21 | Novozymes A/S | Polypeptides having protease activity |
DK3382003T3 (en) | 2011-12-29 | 2021-09-06 | Novozymes As | DETERGENT COMPOSITIONS WITH LIPASE VARIANTS |
WO2013110766A1 (en) | 2012-01-26 | 2013-08-01 | Novozymes A/S | Use of polypeptides having protease activity in animal feed and detergents |
WO2013120948A1 (en) | 2012-02-17 | 2013-08-22 | Novozymes A/S | Subtilisin variants and polynucleotides encoding same |
EP2628785B1 (en) | 2012-02-17 | 2016-05-18 | Henkel AG & Co. KGaA | Detergent compositions comprising subtilase variants |
CN104704102A (en) | 2012-03-07 | 2015-06-10 | 诺维信公司 | Detergent composition and substitution of optical brighteners in detergent compositions |
CN104245926B (en) | 2012-04-27 | 2021-05-07 | 诺维信股份有限公司 | GH61 polypeptide variants and polynucleotides encoding same |
CN104271723B (en) | 2012-05-07 | 2021-04-06 | 诺维信公司 | Polypeptides having xanthan degrading activity and nucleotides encoding same |
BR112014027275A2 (en) | 2012-05-11 | 2017-08-08 | Danisco Us Inc | use of aspergillus clavatus alpha-amylase for saccharification |
JP2015525248A (en) | 2012-05-16 | 2015-09-03 | ノボザイムス アクティーゼルスカブ | Composition comprising lipase and method of use thereof |
WO2014007921A1 (en) | 2012-06-08 | 2014-01-09 | Danisco Us Inc. | Variant alpha amylases with enhanced activity on starch polymers |
US20150184208A1 (en) | 2012-06-19 | 2015-07-02 | Novozymes A/S | Enzymatic reduction of hydroperoxides |
BR112014031882A2 (en) | 2012-06-20 | 2017-08-01 | Novozymes As | use of an isolated polypeptide, polypeptide, composition, isolated polynucleotide, nucleic acid construct or expression vector, recombinant expression host cell, methods for producing a polypeptide, for enhancing the nutritional value of an animal feed, and for the treatment of protein, use of at least one polypeptide, animal feed additive, animal feed, and detergent composition |
US20150218606A1 (en) | 2012-08-16 | 2015-08-06 | Danisco Us Inc. | Method of using alpha-amylase from aspergillus clavatus and pullulanase for saccharification |
MX2015002212A (en) | 2012-08-22 | 2015-05-08 | Novozymes As | Detergent compositions comprising metalloproteases. |
WO2014029819A1 (en) | 2012-08-22 | 2014-02-27 | Novozymes A/S | Metalloprotease from exiguobacterium |
WO2014029821A1 (en) | 2012-08-22 | 2014-02-27 | Novozymes A/S | Metalloproteases from alicyclobacillus sp. |
WO2014081622A1 (en) | 2012-11-20 | 2014-05-30 | Danisco Us Inc. | Amylase with maltogenic properties |
ES2738639T3 (en) | 2012-12-07 | 2020-01-24 | Novozymes As | Bacterial adhesion prevention |
US20160115509A1 (en) | 2012-12-11 | 2016-04-28 | Danisco Us Inc. | Trichoderma reesei host cells expressing a glucoamylase from aspergillus fumigatus and methods of use thereof |
EP2931911A1 (en) | 2012-12-14 | 2015-10-21 | Danisco US Inc. | Method of using alpha-amylase from aspergillus fumigatus and isoamylase for saccharification |
WO2014090940A1 (en) | 2012-12-14 | 2014-06-19 | Novozymes A/S | Removal of skin-derived body soils |
EP2904105A1 (en) | 2012-12-20 | 2015-08-12 | Danisco US Inc. | Method of using alpha-amylase from aspergillus terreus and pullulanase for saccharification |
EP2935575B1 (en) | 2012-12-21 | 2018-04-18 | Danisco US Inc. | Alpha-amylase variants |
WO2014099525A1 (en) | 2012-12-21 | 2014-06-26 | Danisco Us Inc. | Paenibacillus curdlanolyticus amylase, and methods of use, thereof |
MX363360B (en) | 2012-12-21 | 2019-03-21 | Novozymes As | Polypeptides having protease activiy and polynucleotides encoding same. |
CN104903443A (en) | 2013-01-03 | 2015-09-09 | 诺维信公司 | Alpha-amylase variants and polynucleotides encoding same |
US20160017305A1 (en) | 2013-03-11 | 2016-01-21 | Danisco Us Inc. | Alpha-amylase combinatorial variants |
CN105189724A (en) | 2013-03-14 | 2015-12-23 | 诺维信公司 | Enzyme and inhibitor containing water-soluble films |
CN105051174B (en) | 2013-03-21 | 2018-04-03 | 诺维信公司 | Polypeptide and their polynucleotides of coding with lipase active |
MY192746A (en) | 2013-05-14 | 2022-09-06 | Novozymes As | Detergent compositions |
WO2014183921A1 (en) | 2013-05-17 | 2014-11-20 | Novozymes A/S | Polypeptides having alpha amylase activity |
CN105264058B (en) | 2013-06-06 | 2022-03-29 | 诺维信公司 | Alpha-amylase variants and polynucleotides encoding same |
WO2014200658A1 (en) | 2013-06-13 | 2014-12-18 | Danisco Us Inc. | Alpha-amylase from promicromonospora vindobonensis |
WO2014200657A1 (en) | 2013-06-13 | 2014-12-18 | Danisco Us Inc. | Alpha-amylase from streptomyces xiamenensis |
WO2014200656A1 (en) | 2013-06-13 | 2014-12-18 | Danisco Us Inc. | Alpha-amylase from streptomyces umbrinus |
EP3011020A1 (en) | 2013-06-17 | 2016-04-27 | Danisco US Inc. | Alpha-amylase from bacillaceae family member |
US20160145596A1 (en) | 2013-06-27 | 2016-05-26 | Novozymes A/S | Subtilase Variants and Polynucleotides Encoding Same |
EP3013956B1 (en) | 2013-06-27 | 2023-03-01 | Novozymes A/S | Subtilase variants and polynucleotides encoding same |
EP3017032A2 (en) | 2013-07-04 | 2016-05-11 | Novozymes A/S | Polypeptides having anti-redeposition effect and polynucleotides encoding same |
US20160160196A1 (en) | 2013-07-09 | 2016-06-09 | Novozymes A/S | Polypeptides with Lipase Activity And Polynucleotides Encoding Same |
ES2797483T3 (en) | 2013-07-19 | 2020-12-02 | Danisco Us Inc | Compositions and Methods Comprising a Lipolytic Enzyme Variant |
CN105358686A (en) | 2013-07-29 | 2016-02-24 | 诺维信公司 | Protease variants and polynucleotides encoding same |
WO2015014803A1 (en) | 2013-07-29 | 2015-02-05 | Novozymes A/S | Protease variants and polynucleotides encoding same |
EP2832853A1 (en) | 2013-07-29 | 2015-02-04 | Henkel AG&Co. KGAA | Detergent composition comprising protease variants |
EP3052622B1 (en) | 2013-10-03 | 2018-09-19 | Danisco US Inc. | Alpha-amylases from a subset of exiguobacterium, and methods of use, thereof |
WO2015049370A1 (en) | 2013-10-03 | 2015-04-09 | Novozymes A/S | Detergent composition and use of detergent composition |
DK3060659T3 (en) | 2013-10-03 | 2019-09-09 | Danisco Us Inc | ALFA AMYLASES FROM EXIGUOBACTERY AND PROCEDURES FOR USE THEREOF |
JP6560214B2 (en) | 2013-11-20 | 2019-08-14 | ダニスコ・ユーエス・インク | Mutant α-amylase with reduced sensitivity to protease cleavage and method of use thereof |
WO2015094809A1 (en) | 2013-12-19 | 2015-06-25 | Danisco Us Inc. | Chimeric fungal alpha-amylases comprising carbohydrate binding module and the use thereof |
US10030239B2 (en) | 2013-12-20 | 2018-07-24 | Novozymes A/S | Polypeptides having protease activity and polynucleotides encoding same |
WO2015109972A1 (en) | 2014-01-22 | 2015-07-30 | Novozymes A/S | Polypeptides with lipase activity and polynucleotides encoding same |
EP3114272A1 (en) | 2014-03-05 | 2017-01-11 | Novozymes A/S | Compositions and methods for improving properties of cellulosic textile materials with xyloglucan endotransglycosylase |
WO2015134729A1 (en) | 2014-03-05 | 2015-09-11 | Novozymes A/S | Compositions and methods for improving properties of non-cellulosic textile materials with xyloglucan endotransglycosylase |
CN111500552A (en) | 2014-03-12 | 2020-08-07 | 诺维信公司 | Polypeptides having lipase activity and polynucleotides encoding same |
CN106103708A (en) | 2014-04-01 | 2016-11-09 | 诺维信公司 | There is the polypeptide of alpha amylase activity |
CN106170545A (en) | 2014-04-10 | 2016-11-30 | 诺维信公司 | Alpha-amylase variants and the polynucleotide that it is encoded |
MX2016013034A (en) | 2014-04-11 | 2017-02-15 | Novozymes As | Detergent composition. |
EP3131921B1 (en) | 2014-04-15 | 2020-06-10 | Novozymes A/S | Polypeptides with lipase activity and polynucleotides encoding same |
CN106459937A (en) | 2014-05-27 | 2017-02-22 | 诺维信公司 | Methods for producing lipases |
WO2015181119A2 (en) | 2014-05-27 | 2015-12-03 | Novozymes A/S | Lipase variants and polynucleotides encoding same |
EP3155097A1 (en) | 2014-06-12 | 2017-04-19 | Novozymes A/S | Alpha-amylase variants and polynucleotides encoding same |
US9714403B2 (en) | 2014-06-19 | 2017-07-25 | E I Du Pont De Nemours And Company | Compositions containing one or more poly alpha-1,3-glucan ether compounds |
EP3158043B1 (en) | 2014-06-19 | 2021-03-10 | Nutrition & Biosciences USA 4, Inc. | Compositions containing one or more poly alpha-1,3-glucan ether compounds |
EP3140399B1 (en) | 2014-07-04 | 2018-03-28 | Novozymes A/S | Subtilase variants and polynucleotides encoding same |
US10626388B2 (en) | 2014-07-04 | 2020-04-21 | Novozymes A/S | Subtilase variants and polynucleotides encoding same |
WO2016079110A2 (en) | 2014-11-19 | 2016-05-26 | Novozymes A/S | Use of enzyme for cleaning |
CN107075489A (en) | 2014-11-20 | 2017-08-18 | 诺维信公司 | Alicyclic acid bacillus variant and the polynucleotides for encoding them |
EP3227444B1 (en) | 2014-12-04 | 2020-02-12 | Novozymes A/S | Subtilase variants and polynucleotides encoding same |
CN107002054A (en) | 2014-12-05 | 2017-08-01 | 诺维信公司 | Lipase Variant and the polynucleotides for encoding them |
ES2763235T3 (en) | 2014-12-15 | 2020-05-27 | Henkel Ag & Co Kgaa | Detergent composition comprising subtilase variants |
WO2016096996A1 (en) | 2014-12-16 | 2016-06-23 | Novozymes A/S | Polypeptides having n-acetyl glucosamine oxidase activity |
US10400230B2 (en) | 2014-12-19 | 2019-09-03 | Novozymes A/S | Protease variants and polynucleotides encoding same |
ES2813727T3 (en) | 2014-12-19 | 2021-03-24 | Novozymes As | Protease variants and polynucleotides that encode them |
US20180112156A1 (en) | 2015-04-10 | 2018-04-26 | Novozymes A/S | Laundry method, use of polypeptide and detergent composition |
EP3280800A1 (en) | 2015-04-10 | 2018-02-14 | Novozymes A/S | Detergent composition |
EP3298121B1 (en) | 2015-05-19 | 2019-03-20 | Novozymes A/S | Odor reduction |
WO2016202739A1 (en) | 2015-06-16 | 2016-12-22 | Novozymes A/S | Polypeptides with lipase activity and polynucleotides encoding same |
EP3310912B1 (en) | 2015-06-18 | 2021-01-27 | Novozymes A/S | Subtilase variants and polynucleotides encoding same |
EP3106508B1 (en) | 2015-06-18 | 2019-11-20 | Henkel AG & Co. KGaA | Detergent composition comprising subtilase variants |
EP3317388B1 (en) | 2015-06-30 | 2019-11-13 | Novozymes A/S | Laundry detergent composition, method for washing and use of composition |
CN107922930A (en) | 2015-07-01 | 2018-04-17 | 诺维信公司 | The method for reducing smell |
WO2017005816A1 (en) | 2015-07-06 | 2017-01-12 | Novozymes A/S | Lipase variants and polynucleotides encoding same |
PL3350303T3 (en) | 2015-09-17 | 2021-01-25 | Henkel Ag & Co. Kgaa | Detergent compositions comprising polypeptides having xanthan degrading activity |
CN108350443B (en) | 2015-09-17 | 2022-06-28 | 诺维信公司 | Polypeptides having xanthan degrading activity and polynucleotides encoding same |
CN108350441B (en) | 2015-10-07 | 2022-09-27 | 诺维信公司 | Polypeptides |
CN108291215A (en) | 2015-10-14 | 2018-07-17 | 诺维信公司 | Polypeptide with proteinase activity and encode their polynucleotides |
EP4324919A3 (en) | 2015-10-14 | 2024-05-29 | Novozymes A/S | Polypeptide variants |
US11028346B2 (en) | 2015-10-28 | 2021-06-08 | Novozymes A/S | Detergent composition comprising protease and amylase variants |
US11001821B2 (en) | 2015-11-24 | 2021-05-11 | Novozymes A/S | Polypeptides having protease activity and polynucleotides encoding same |
US10870838B2 (en) | 2015-12-01 | 2020-12-22 | Novozymes A/S | Methods for producing lipases |
CN108779448B (en) | 2015-12-09 | 2023-08-18 | 丹尼斯科美国公司 | Alpha-amylase combination variants |
EP3397761B1 (en) | 2015-12-30 | 2022-11-09 | Novozymes A/S | Enzyme variants and polynucleotides encoding the same |
US20210171927A1 (en) | 2016-01-29 | 2021-06-10 | Novozymes A/S | Beta-glucanase variants and polynucleotides encoding same |
EP3433347B1 (en) | 2016-03-23 | 2020-05-06 | Novozymes A/S | Use of polypeptide having dnase activity for treating fabrics |
WO2017173190A2 (en) | 2016-04-01 | 2017-10-05 | Danisco Us Inc. | Alpha-amylases, compositions & methods |
WO2017173324A2 (en) | 2016-04-01 | 2017-10-05 | Danisco Us Inc. | Alpha-amylases, compositions & methods |
US20200325418A1 (en) | 2016-04-08 | 2020-10-15 | Novozymes A/S | Detergent compositions and uses of the same |
JP6959259B2 (en) | 2016-04-29 | 2021-11-02 | ノボザイムス アクティーゼルスカブ | Detergent composition and its use |
WO2017191160A1 (en) | 2016-05-03 | 2017-11-09 | Novozymes A/S | Alpha-amylase variants and polynucleotides encoding the same |
CA3022121A1 (en) | 2016-05-09 | 2017-11-16 | Novozymes A/S | Variant polypeptides with improved performance and use of the same |
US11058129B2 (en) | 2016-05-24 | 2021-07-13 | Novozymes A/S | Animal feed additives |
AU2017269498A1 (en) | 2016-05-24 | 2018-11-08 | Novozymes A/S | Polypeptides having alpha-galactosidase activity and polynucleotides encoding same |
CN109312321A (en) | 2016-05-24 | 2019-02-05 | 诺维信公司 | Composition comprising the polypeptide with galactanase activity and the polypeptide with betagalactosidase activity |
BR112018073283A2 (en) | 2016-05-24 | 2019-03-19 | Novozymes A/S | composition, granule, feed additive, feed, pelleted feed, liquid formulation, method for releasing galactose from plant-based material, method for improving one or more performance parameters of an animal, use of the composition, granule, animal feed additive or liquid formulation, isolated polypeptide, method for producing the polypeptide, polynucleotide, nucleic acid construct or expression vector, and host cell |
EP3464582A1 (en) | 2016-06-03 | 2019-04-10 | Novozymes A/S | Subtilase variants and polynucleotides encoding same |
US11203732B2 (en) | 2016-06-30 | 2021-12-21 | Novozymes A/S | Lipase variants and compositions comprising surfactant and lipase variant |
WO2018002261A1 (en) | 2016-07-01 | 2018-01-04 | Novozymes A/S | Detergent compositions |
EP3481949B1 (en) | 2016-07-05 | 2021-06-09 | Novozymes A/S | Pectate lyase variants and polynucleotides encoding same |
WO2018007573A1 (en) | 2016-07-08 | 2018-01-11 | Novozymes A/S | Detergent compositions with galactanase |
AU2017294066A1 (en) | 2016-07-08 | 2019-01-17 | Novozymes A/S | Polypeptides having xylanase activity and polynucleotides encoding same |
AR108861A1 (en) | 2016-07-08 | 2018-10-03 | Novozymes As | XYLANASE AND POLYNUCLEOTIDE VARIANTS CODING THEM |
WO2018011276A1 (en) | 2016-07-13 | 2018-01-18 | The Procter & Gamble Company | Bacillus cibi dnase variants and uses thereof |
EP4357453A2 (en) | 2016-07-18 | 2024-04-24 | Novozymes A/S | Lipase variants, polynucleotides encoding same and the use thereof |
WO2018037065A1 (en) | 2016-08-24 | 2018-03-01 | Henkel Ag & Co. Kgaa | Detergent composition comprising gh9 endoglucanase variants i |
CN109863244B (en) | 2016-08-24 | 2023-06-06 | 诺维信公司 | GH9 endoglucanase variants and polynucleotides encoding same |
WO2018037061A1 (en) | 2016-08-24 | 2018-03-01 | Novozymes A/S | Xanthan lyase variants and polynucleotides encoding same |
AU2017317563B8 (en) | 2016-08-24 | 2023-03-23 | Henkel Ag & Co. Kgaa | Detergent compositions comprising xanthan lyase variants I |
EP3532592A1 (en) | 2016-10-25 | 2019-09-04 | Novozymes A/S | Detergent compositions |
WO2018108865A1 (en) | 2016-12-12 | 2018-06-21 | Novozymes A/S | Use of polypeptides |
CN110662836B (en) | 2017-03-31 | 2024-04-12 | 丹尼斯科美国公司 | Alpha-amylase combination variants |
WO2018185181A1 (en) | 2017-04-04 | 2018-10-11 | Novozymes A/S | Glycosyl hydrolases |
US20200109352A1 (en) | 2017-04-04 | 2020-04-09 | Novozymes A/S | Polypeptide compositions and uses thereof |
DK3385361T3 (en) | 2017-04-05 | 2019-06-03 | Ab Enzymes Gmbh | Detergent compositions comprising bacterial mannanases |
EP3385362A1 (en) | 2017-04-05 | 2018-10-10 | Henkel AG & Co. KGaA | Detergent compositions comprising fungal mannanases |
WO2018185269A1 (en) | 2017-04-06 | 2018-10-11 | Novozymes A/S | Cleaning compositions and uses thereof |
EP3607037A1 (en) | 2017-04-06 | 2020-02-12 | Novozymes A/S | Cleaning compositions and uses thereof |
MX2019011764A (en) | 2017-04-06 | 2019-11-28 | Novozymes As | Cleaning compositions and uses thereof. |
WO2018185280A1 (en) | 2017-04-06 | 2018-10-11 | Novozymes A/S | Cleaning compositions and uses thereof |
WO2018185267A1 (en) | 2017-04-06 | 2018-10-11 | Novozymes A/S | Cleaning compositions and uses thereof |
WO2018185285A1 (en) | 2017-04-06 | 2018-10-11 | Novozymes A/S | Cleaning compositions and uses thereof |
US11078445B2 (en) | 2017-05-05 | 2021-08-03 | Novozymes A/S | Compositions comprising lipase and sulfite |
WO2018206535A1 (en) | 2017-05-08 | 2018-11-15 | Novozymes A/S | Carbohydrate-binding domain and polynucleotides encoding the same |
EP3401385A1 (en) | 2017-05-08 | 2018-11-14 | Henkel AG & Co. KGaA | Detergent composition comprising polypeptide comprising carbohydrate-binding domain |
US11492605B2 (en) | 2017-05-08 | 2022-11-08 | Novozymes A/S | Mannanase variants and polynucleotides encoding same |
CN110741084B (en) | 2017-05-08 | 2024-04-12 | 诺维信公司 | Mannanase variants and polynucleotides encoding same |
WO2018224544A1 (en) | 2017-06-08 | 2018-12-13 | Novozymes A/S | Compositions comprising polypeptides having cellulase activity and amylase activity, and uses thereof in cleaning and detergent compositions |
US11499144B2 (en) | 2017-06-22 | 2022-11-15 | Novozymes A/S | Xylanase variants and polynucleotides encoding same |
EP3673057A1 (en) | 2017-08-24 | 2020-07-01 | Novozymes A/S | Xanthan lyase variants and polynucleotides encoding same |
WO2019038060A1 (en) | 2017-08-24 | 2019-02-28 | Henkel Ag & Co. Kgaa | Detergent composition comprising xanthan lyase variants ii |
WO2019038058A1 (en) | 2017-08-24 | 2019-02-28 | Novozymes A/S | Gh9 endoglucanase variants and polynucleotides encoding same |
EP3673056A1 (en) | 2017-08-24 | 2020-07-01 | Henkel AG & Co. KGaA | Detergent compositions comprising gh9 endoglucanase variants ii |
EP3675646A1 (en) | 2017-09-01 | 2020-07-08 | Novozymes A/S | Animal feed additives comprising polypeptide having protease activity and uses thereof |
EP3675647A1 (en) | 2017-09-01 | 2020-07-08 | Novozymes A/S | Animal feed additives comprising a polypeptide having protease activity and uses thereof |
EP3684899A1 (en) | 2017-09-22 | 2020-07-29 | Novozymes A/S | Novel polypeptides |
JP7114697B2 (en) | 2017-09-27 | 2022-08-08 | ザ プロクター アンド ギャンブル カンパニー | Detergent composition containing lipase |
WO2019063499A1 (en) | 2017-09-27 | 2019-04-04 | Novozymes A/S | Lipase variants and microcapsule compositions comprising such lipase variants |
US11746310B2 (en) | 2017-10-02 | 2023-09-05 | Novozymes A/S | Polypeptides having mannanase activity and polynucleotides encoding same |
EP3692148A1 (en) | 2017-10-02 | 2020-08-12 | Novozymes A/S | Polypeptides having mannanase activity and polynucleotides encoding same |
WO2019076800A1 (en) | 2017-10-16 | 2019-04-25 | Novozymes A/S | Cleaning compositions and uses thereof |
EP3701001A1 (en) | 2017-10-24 | 2020-09-02 | Novozymes A/S | Compositions comprising polypeptides having mannanase activity |
CN117683748A (en) | 2017-10-27 | 2024-03-12 | 宝洁公司 | Detergent compositions comprising polypeptide variants |
WO2019081721A1 (en) | 2017-10-27 | 2019-05-02 | Novozymes A/S | Dnase variants |
US20200291330A1 (en) | 2017-11-01 | 2020-09-17 | Novozymes A/S | Polypeptides and Compositions Comprising Such Polypeptides |
DE102017125560A1 (en) | 2017-11-01 | 2019-05-02 | Henkel Ag & Co. Kgaa | CLEANSING COMPOSITIONS CONTAINING DISPERSINE III |
DE102017125558A1 (en) | 2017-11-01 | 2019-05-02 | Henkel Ag & Co. Kgaa | CLEANING COMPOSITIONS CONTAINING DISPERSINE I |
EP4379029A1 (en) | 2017-11-01 | 2024-06-05 | Novozymes A/S | Polypeptides and compositions comprising such polypeptides |
US11725197B2 (en) | 2017-12-04 | 2023-08-15 | Novozymes A/S | Lipase variants and polynucleotides encoding same |
EP3727024A1 (en) | 2017-12-20 | 2020-10-28 | DSM IP Assets B.V. | Animal feed compositions comprising muramidase and uses thereof |
WO2019121930A1 (en) | 2017-12-20 | 2019-06-27 | Dsm Ip Assets B.V. | Animal feed compositions and uses thereof |
CN111868251A (en) | 2018-01-11 | 2020-10-30 | 诺维信公司 | Animal feed composition and use thereof |
WO2019157061A2 (en) | 2018-02-06 | 2019-08-15 | Novozymes Bioag A/S | Methods of protecting a plant from fungal pests |
WO2019154951A1 (en) | 2018-02-08 | 2019-08-15 | Novozymes A/S | Lipases, lipase variants and compositions thereof |
CN111757930A (en) | 2018-02-08 | 2020-10-09 | 诺维信公司 | Lipase variants and compositions thereof |
WO2019162000A1 (en) | 2018-02-23 | 2019-08-29 | Henkel Ag & Co. Kgaa | Detergent composition comprising xanthan lyase and endoglucanase variants |
US11535837B2 (en) | 2018-03-29 | 2022-12-27 | Novozymes A/S | Mannanase variants and polynucleotides encoding same |
WO2019201793A1 (en) | 2018-04-17 | 2019-10-24 | Novozymes A/S | Polypeptides comprising carbohydrate binding activity in detergent compositions and their use in reducing wrinkles in textile or fabric. |
WO2019201785A1 (en) | 2018-04-19 | 2019-10-24 | Novozymes A/S | Stabilized cellulase variants |
CN112272701B (en) | 2018-04-19 | 2024-05-14 | 诺维信公司 | Stabilized cellulase variants |
BR112020021365A2 (en) | 2018-04-25 | 2021-01-19 | Novozymes A/S | ANIMAL FEED, METHOD FOR IMPROVING THE EUROPEAN PRODUCTION EFFICIENCY FACTOR, BODY WEIGHT GAIN AND / OR RATION CONVERSION REASON FOR A MONOGRAPHIC ANIMAL, USE OF AT LEAST ONE PROBIOTIC IN COMBINATION WITH A POLYPEPTIOUS ACTIVITY OF BEING ACTIVELY ACTIVE IN HIS ACTIVITY. FEED, AND, FEED COMPOSITION OR PRE-MIXTURE COMPOSITION, OR ANIMAL FEED ADDITIVE. |
BR112020024509A2 (en) | 2018-06-05 | 2021-03-02 | Novozymes Bioag A/S | methods of foliar application of a composition, of controlling plant pests on a plant or part of the plant and / or inducing resistance to a plant pest on a plant or part of the plant and of controlling or preventing pest damage in a plant plant propagation material, a plant, part of a plant and / or plant organ. |
CA3101519A1 (en) | 2018-06-05 | 2019-12-12 | Novozymes Bioag A/S | Methods of protecting a plant from insect pests |
US12012573B2 (en) | 2018-07-02 | 2024-06-18 | Novozymes A/S | Cleaning compositions and uses thereof |
WO2020007875A1 (en) | 2018-07-03 | 2020-01-09 | Novozymes A/S | Cleaning compositions and uses thereof |
WO2020008024A1 (en) | 2018-07-06 | 2020-01-09 | Novozymes A/S | Cleaning compositions and uses thereof |
US20210253981A1 (en) | 2018-07-06 | 2021-08-19 | Novozymes A/S | Cleaning compositions and uses thereof |
CN112566502A (en) | 2018-08-31 | 2021-03-26 | 诺维信公司 | Polypeptides having protease activity and polynucleotides encoding same |
US20220054600A1 (en) | 2018-09-17 | 2022-02-24 | Dsm Ip Assets B.V. | Animal feed compositions and uses thereof |
MX2021003040A (en) | 2018-09-17 | 2021-07-15 | Dsm Ip Assets Bv | Animal feed compositions and uses thereof. |
US20220040271A1 (en) | 2018-09-17 | 2022-02-10 | Dsm Ip Assets B.V. | Animal feed compositions and uses thereof |
MX2021003035A (en) | 2018-09-17 | 2021-08-11 | Dsm Ip Assets Bv | Animal feed compositions and uses thereof. |
US20230287306A1 (en) | 2018-10-02 | 2023-09-14 | Novozymes A/S | Cleaning Composition |
US20220073845A1 (en) | 2018-10-02 | 2022-03-10 | Novozymes A/S | Endonuclease 1 ribonucleases for cleaning |
WO2020070209A1 (en) | 2018-10-02 | 2020-04-09 | Novozymes A/S | Cleaning composition |
WO2020070199A1 (en) | 2018-10-03 | 2020-04-09 | Novozymes A/S | Polypeptides having alpha-mannan degrading activity and polynucleotides encoding same |
EP3864123A1 (en) | 2018-10-09 | 2021-08-18 | Novozymes A/S | Cleaning compositions and uses thereof |
WO2020074498A1 (en) | 2018-10-09 | 2020-04-16 | Novozymes A/S | Cleaning compositions and uses thereof |
US20220033739A1 (en) | 2018-10-11 | 2022-02-03 | Novozymes A/S | Cleaning compositions and uses thereof |
EP3647398B1 (en) | 2018-10-31 | 2024-05-15 | Henkel AG & Co. KGaA | Cleaning compositions containing dispersins v |
EP3647397A1 (en) | 2018-10-31 | 2020-05-06 | Henkel AG & Co. KGaA | Cleaning compositions containing dispersins iv |
EP3898962A2 (en) | 2018-12-21 | 2021-10-27 | Novozymes A/S | Polypeptides having peptidoglycan degrading activity and polynucleotides encoding same |
DE102019200138A1 (en) | 2019-01-08 | 2020-07-09 | Beiersdorf Ag | Preparation with cellulose particles coated with vinylamine / N-vinylformamide copolymer |
DE102019200135A1 (en) | 2019-01-08 | 2020-07-09 | Beiersdorf Ag | Preparation with silica particles coated with vinylamine / N-vinylformamide copolymer |
EP3942032A1 (en) | 2019-03-21 | 2022-01-26 | Novozymes A/S | Alpha-amylase variants and polynucleotides encoding same |
EP3947619A1 (en) | 2019-04-03 | 2022-02-09 | Novozymes A/S | Polypeptides having beta-glucanase activity, polynucleotides encoding same and uses thereof in cleaning and detergent compositions |
CN113874499A (en) | 2019-04-10 | 2021-12-31 | 诺维信公司 | Polypeptide variants |
EP3953463A1 (en) | 2019-04-12 | 2022-02-16 | Novozymes A/S | Stabilized glycoside hydrolase variants |
EP3994255A1 (en) | 2019-07-02 | 2022-05-11 | Novozymes A/S | Lipase variants and compositions thereof |
WO2021030400A1 (en) | 2019-08-13 | 2021-02-18 | Novozymes Bioag A/S | Pesticidal combinations of yersinia and proteases |
CN114787329A (en) | 2019-08-27 | 2022-07-22 | 诺维信公司 | Detergent composition |
CN114555769A (en) | 2019-08-27 | 2022-05-27 | 诺维信公司 | Compositions comprising lipase |
EP4031661A1 (en) | 2019-09-16 | 2022-07-27 | Novozymes A/S | Polypeptides having beta-glucanase activity and polynucleotides encoding same |
EP4031644A1 (en) | 2019-09-19 | 2022-07-27 | Novozymes A/S | Detergent composition |
EP4038170A1 (en) | 2019-10-03 | 2022-08-10 | Novozymes A/S | Polypeptides comprising at least two carbohydrate binding domains |
WO2021078839A1 (en) | 2019-10-22 | 2021-04-29 | Novozymes A/S | Animal feed composition |
WO2021122118A1 (en) | 2019-12-20 | 2021-06-24 | Henkel Ag & Co. Kgaa | Cleaning compositions comprising dispersins vi |
US20220411773A1 (en) | 2019-12-20 | 2022-12-29 | Novozymes A/S | Polypeptides having proteolytic activity and use thereof |
US20230045289A1 (en) | 2019-12-20 | 2023-02-09 | Henkel Ag & Co. Kgaa | Cleaning compositions comprising dispersins ix |
KR20220121235A (en) | 2019-12-20 | 2022-08-31 | 헨켈 아게 운트 코. 카게아아 | Cleaning Composition Comprising Dispersin and Carbohydrase |
EP4077621A2 (en) | 2019-12-20 | 2022-10-26 | Henkel AG & Co. KGaA | Cleaning compositions comprising dispersins viii |
WO2021130167A1 (en) | 2019-12-23 | 2021-07-01 | Novozymes A/S | Enzyme compositions and uses thereof |
EP4093842A1 (en) | 2020-01-23 | 2022-11-30 | Novozymes A/S | Enzyme compositions and uses thereof |
EP4097227A1 (en) | 2020-01-31 | 2022-12-07 | Novozymes A/S | Mannanase variants and polynucleotides encoding same |
EP4097226A1 (en) | 2020-01-31 | 2022-12-07 | Novozymes A/S | Mannanase variants and polynucleotides encoding same |
EP4103709A2 (en) | 2020-02-10 | 2022-12-21 | Novozymes A/S | Polypeptides having alpha-amylase activity and polynucleotides encoding same |
EP3892708A1 (en) | 2020-04-06 | 2021-10-13 | Henkel AG & Co. KGaA | Cleaning compositions comprising dispersin variants |
MX2022011948A (en) | 2020-04-08 | 2022-10-21 | Novozymes As | Carbohydrate binding module variants. |
EP4139431A1 (en) | 2020-04-21 | 2023-03-01 | Novozymes A/S | Cleaning compositions comprising polypeptides having fructan degrading activity |
BR112022023230A2 (en) | 2020-05-18 | 2022-12-27 | Dsm Ip Assets Bv | ANIMAL FEED COMPOSITIONS |
EP4152945A1 (en) | 2020-05-18 | 2023-03-29 | DSM IP Assets B.V. | Animal feed compositions |
EP3936593A1 (en) | 2020-07-08 | 2022-01-12 | Henkel AG & Co. KGaA | Cleaning compositions and uses thereof |
JP2023538740A (en) | 2020-08-25 | 2023-09-11 | ノボザイムス アクティーゼルスカブ | Variants of family 44 xyloglucanase |
CN116507725A (en) | 2020-10-07 | 2023-07-28 | 诺维信公司 | Alpha-amylase variants |
AU2021358426A1 (en) | 2020-10-07 | 2023-05-25 | Novozymes A/S | Enzymatic preservation of probiotics in animal feed |
EP4228424A1 (en) | 2020-10-15 | 2023-08-23 | DSM IP Assets B.V. | Methods of modulating gastrointestinal metabolites |
WO2022084303A2 (en) | 2020-10-20 | 2022-04-28 | Novozymes A/S | Use of polypeptides having dnase activity |
US20230399588A1 (en) | 2020-10-28 | 2023-12-14 | Novozymes A/S | Use of lipoxygenase |
JP2023547450A (en) | 2020-10-29 | 2023-11-10 | ノボザイムス アクティーゼルスカブ | Lipase variants and compositions comprising such lipase variants |
MX2023004938A (en) | 2020-11-02 | 2023-05-17 | Novozymes As | Glucoamylase variants and polynucleotides encoding same. |
WO2022103725A1 (en) | 2020-11-13 | 2022-05-19 | Novozymes A/S | Detergent composition comprising a lipase |
WO2022106404A1 (en) | 2020-11-18 | 2022-05-27 | Novozymes A/S | Combination of proteases |
WO2022106400A1 (en) | 2020-11-18 | 2022-05-27 | Novozymes A/S | Combination of immunochemically different proteases |
EP4039806A1 (en) | 2021-02-04 | 2022-08-10 | Henkel AG & Co. KGaA | Detergent composition comprising xanthan lyase and endoglucanase variants with im-proved stability |
CN116829709A (en) | 2021-02-12 | 2023-09-29 | 诺维信公司 | Alpha-amylase variants |
EP4060036A1 (en) | 2021-03-15 | 2022-09-21 | Novozymes A/S | Polypeptide variants |
WO2022194673A1 (en) | 2021-03-15 | 2022-09-22 | Novozymes A/S | Dnase variants |
EP4359518A1 (en) | 2021-06-23 | 2024-05-01 | Novozymes A/S | Alpha-amylase polypeptides |
WO2023288294A1 (en) | 2021-07-16 | 2023-01-19 | Novozymes A/S | Compositions and methods for improving the rainfastness of proteins on plant surfaces |
WO2023061928A1 (en) | 2021-10-12 | 2023-04-20 | Novozymes A/S | Endoglucanase with improved stability |
WO2023116569A1 (en) | 2021-12-21 | 2023-06-29 | Novozymes A/S | Composition comprising a lipase and a booster |
EP4234664A1 (en) | 2022-02-24 | 2023-08-30 | Evonik Operations GmbH | Composition comprising glucolipids and enzymes |
WO2023165507A1 (en) | 2022-03-02 | 2023-09-07 | Novozymes A/S | Use of xyloglucanase for improvement of sustainability of detergents |
WO2023165950A1 (en) | 2022-03-04 | 2023-09-07 | Novozymes A/S | Dnase variants and compositions |
AU2023231428A1 (en) | 2022-03-08 | 2024-07-11 | Novozymes A/S | Fusion polypeptides with deamidase inhibitor and deamidase domains |
EP4242303A1 (en) | 2022-03-08 | 2023-09-13 | Novozymes A/S | Fusion polypeptides with deamidase inhibitor and deamidase domains |
WO2023194388A1 (en) | 2022-04-07 | 2023-10-12 | Novozymes A/S | Fusion proteins and their use against eimeria |
WO2023194204A1 (en) | 2022-04-08 | 2023-10-12 | Novozymes A/S | Hexosaminidase variants and compositions |
WO2023225459A2 (en) | 2022-05-14 | 2023-11-23 | Novozymes A/S | Compositions and methods for preventing, treating, supressing and/or eliminating phytopathogenic infestations and infections |
WO2023247348A1 (en) | 2022-06-21 | 2023-12-28 | Novozymes A/S | Mannanase variants and polynucleotides encoding same |
WO2023247664A2 (en) | 2022-06-24 | 2023-12-28 | Novozymes A/S | Lipase variants and compositions comprising such lipase variants |
WO2024003143A1 (en) | 2022-06-30 | 2024-01-04 | Novozymes A/S | Mutanases and oral care compositions comprising same |
WO2024012912A1 (en) | 2022-07-15 | 2024-01-18 | Novozymes A/S | Polypeptides having deamidase inhibitor activity |
WO2024083819A1 (en) | 2022-10-20 | 2024-04-25 | Novozymes A/S | Lipid removal in detergents |
WO2024121070A1 (en) | 2022-12-05 | 2024-06-13 | Novozymes A/S | Protease variants and polynucleotides encoding same |
WO2024121058A1 (en) | 2022-12-05 | 2024-06-13 | Novozymes A/S | A composition comprising a lipase and a peptide |
WO2024121324A1 (en) | 2022-12-08 | 2024-06-13 | Novozymes A/S | Polypeptide having lysozyme activity and polynucleotides encoding same |
WO2024126483A1 (en) | 2022-12-14 | 2024-06-20 | Novozymes A/S | Improved lipase (gcl1) variants |
WO2024137246A1 (en) | 2022-12-19 | 2024-06-27 | Novozymes A/S | Carbohydrate esterase family 1 (ce1) polypeptides having ferulic acid esterase and/or acetyl xylan esterase activity and polynucleotides encoding same |
WO2024137250A1 (en) | 2022-12-19 | 2024-06-27 | Novozymes A/S | Carbohydrate esterase family 3 (ce3) polypeptides having acetyl xylan esterase activity and polynucleotides encoding same |
WO2024133495A1 (en) | 2022-12-21 | 2024-06-27 | Novozymes A/S | Microbial proteases for cell detachment |
EP4389865A1 (en) | 2022-12-21 | 2024-06-26 | Novozymes A/S | Recombinant protease for cell detachment |
WO2024133497A1 (en) | 2022-12-21 | 2024-06-27 | Novozymes A/S | Recombinant protease for cell detachment |
WO2024131880A2 (en) | 2022-12-23 | 2024-06-27 | Novozymes A/S | Detergent composition comprising catalase and amylase |
-
1973
- 1973-07-23 GB GB34993/73A patent/GB1483591A/en not_active Expired
-
1974
- 1974-07-12 CH CH965874A patent/CH604923A5/xx not_active IP Right Cessation
- 1974-07-17 NL NL7409683A patent/NL7409683A/en not_active Application Discontinuation
- 1974-07-17 DK DK384574A patent/DK384574A/da not_active Application Discontinuation
- 1974-07-18 FI FI2194/74A patent/FI219474A/fi unknown
- 1974-07-19 SE SE7409471A patent/SE7409471L/xx unknown
- 1974-07-20 DE DE2435008A patent/DE2435008A1/en not_active Ceased
- 1974-07-22 CA CA205,367A patent/CA1049334A/en not_active Expired
- 1974-07-22 BE BE146802A patent/BE817930A/en not_active IP Right Cessation
- 1974-07-22 IT IT52219/74A patent/IT1016947B/en active
- 1974-07-22 ES ES428475A patent/ES428475A1/en not_active Expired
- 1974-07-23 AU AU71557/74A patent/AU498649B2/en not_active Expired
- 1974-07-23 JP JP49084519A patent/JPS5071583A/ja active Pending
- 1974-07-23 IE IE1568/74A patent/IE41403B1/en unknown
- 1974-07-23 AT AT606874A patent/AT357979B/en active
- 1974-07-23 FR FR7425523A patent/FR2238530B1/fr not_active Expired
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4828882A (en) * | 1987-03-16 | 1989-05-09 | Canadian Patents & Developments Limited | Particle encapsulation technique |
US5211985A (en) * | 1991-10-09 | 1993-05-18 | Ici Canada, Inc. | Multi-stage process for continuous coating of fertilizer particles |
US5399186A (en) * | 1991-10-09 | 1995-03-21 | Ici Canada, Inc. | Apparatus and process for coating particles |
Also Published As
Publication number | Publication date |
---|---|
BE817930A (en) | 1975-01-22 |
FR2238530A1 (en) | 1975-02-21 |
AU498649B2 (en) | 1979-03-22 |
CH604923A5 (en) | 1978-09-15 |
ATA606874A (en) | 1980-01-15 |
AT357979B (en) | 1980-08-11 |
GB1483591A (en) | 1977-08-24 |
IE41403L (en) | 1975-01-23 |
IE41403B1 (en) | 1980-01-02 |
DK384574A (en) | 1975-03-03 |
IT1016947B (en) | 1977-06-20 |
FR2238530B1 (en) | 1979-03-09 |
SE7409471L (en) | 1975-01-24 |
AU7155774A (en) | 1976-01-29 |
DE2435008A1 (en) | 1975-02-06 |
NL7409683A (en) | 1975-01-27 |
FI219474A (en) | 1975-01-24 |
ES428475A1 (en) | 1976-12-16 |
JPS5071583A (en) | 1975-06-13 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CA1049334A (en) | Process for coating water soluble or water dispersible particles by means of the fluid bed technique | |
US5422121A (en) | Oral dosage unit form | |
Porter | Controlled-release film coatings based on ethylcellulose | |
US4106991A (en) | Enzyme granulate composition and process for forming enzyme granulates | |
US4689297A (en) | Dust free particulate enzyme formulation | |
EP0035780B1 (en) | Coating compositions for enterosoluble solid dosage forms | |
DE60223148T2 (en) | GRANULATE WITH HIGH STRIKE STRENGTH | |
DE60026970T2 (en) | COMPOSITIONS OF LOW DENSITY AND PARTICLES OF THESE CONTAIN | |
US8535924B2 (en) | Granules with reduced dust potential comprising an antifoam agent | |
US5851579A (en) | Aqueous enteric coating compositions | |
US5846798A (en) | Multi-enzyme granules | |
DE102004021384A1 (en) | Process for the production of granules with improved storage stability and abrasion resistance | |
EP0648487A1 (en) | Dispersion of enteric coating agent | |
DE4310506A1 (en) | Enzyme preparation for detergents and cleaning agents | |
HU186475B (en) | Coating material soluble or swelling in gastric fluids further process for coating pharmaceutical compositions | |
WO1994026883A2 (en) | Process for dust-free enzyme manufacture | |
WO1994026883A9 (en) | Process for dust-free enzyme manufacture | |
WO1992004408A1 (en) | Shaped articles as obtained from a thermoplastic starch melt | |
US8865432B2 (en) | Method for preparing cellulose derivatives having solubility improved | |
US5811121A (en) | PH-sensitive coatings based on cellulose acetoacetate | |
US3854981A (en) | Process for embedding or enveloping solid materials | |
CN101686714B (en) | In situ, liquid-activated film coated tablets and process for making same | |
JPH03111497A (en) | Coating of particle for compounding into detergent | |
JPS60215003A (en) | Chitosan molding and its production | |
US5326586A (en) | Coating of drug forms |