DE2435008A1 - PROCESS FOR COVERING WATER-SOLUBLE OR DISPERSIBLE PARTICLES ACCORDING TO FLOW-BED TECHNOLOGY - Google Patents
PROCESS FOR COVERING WATER-SOLUBLE OR DISPERSIBLE PARTICLES ACCORDING TO FLOW-BED TECHNOLOGYInfo
- Publication number
- DE2435008A1 DE2435008A1 DE2435008A DE2435008A DE2435008A1 DE 2435008 A1 DE2435008 A1 DE 2435008A1 DE 2435008 A DE2435008 A DE 2435008A DE 2435008 A DE2435008 A DE 2435008A DE 2435008 A1 DE2435008 A1 DE 2435008A1
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- DE
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- Prior art keywords
- coating
- particles
- coated
- water
- coating agent
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Classifications
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11D—DETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
- C11D3/00—Other compounding ingredients of detergent compositions covered in group C11D1/00
- C11D3/16—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
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- 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
Description
DifL-his. FRANZ LOHRENTZ 8500 NORNBERQDifL-his. FRANZ LOHRENTZ 8500 NORNBERQ
Novo Terapeutisk Laboratorium A/S, DK-2880 Bagsvard, DänemarkNovo Terapeutisk Laboratorium A / S, DK-2880 Bagsvard, Denmark
Verfahren zum Überziehen von in Wasser löslichen oder dispergierbaren Partikeln nach der Fliessbettechnik ; Process for coating particles which are soluble or dispersible in water using the fluidized bed technique ;
Die Erfindung bezieht sich auf ein Verfahren zum Überziehen von in Wasser löslichen oder in Wasser dispergierbaren Partikeln nach der Fliessbettechnik.The invention relates to a method for coating water-soluble or water-dispersible particles according to the fluid bed technology.
Es ist bekannt, die verschiedensten aus einzelnen Partikeln bestehenden Produkte mit einer Partikelgrösse von weniger als etwa 10 mm, vorzugsweise weniger als 1 mm, mit einem überzug zu versehen, um so die Abriebbildung herabzusetzen, beispielsweise bei Enzyme enthaltenden Zusätzen für in Pulverform vorliegenden Detergentien. Erfahrungsgemäss treten hierbei beträchtliche Schwierigkeiten auf. In der Praxis ist man bisher so vorgegangen, dass beim Überziehen von wasserlöslichen Partikeln in organischen Lösungsmitteln und nicht in Wasser aufgelöste Überzugsagenzien eingesetzt wurden. Die organischen Lösungsmittel müssen abgedampft und im Verlaufe des Verfahrens wiedergewonnen werden, was Feuergefahr undIt is known that the most varied of individual particle products with a particle size of less than about 10 mm, preferably less than 1 mm, with a coating to be provided in order to reduce the formation of abrasion, for example in the case of additives containing enzymes for in powder form present detergents. Experience has shown that this occurs considerable difficulties. In practice, the procedure so far has been that when coating water-soluble Particles in organic solvents and coating agents not dissolved in water were used. the Organic solvents must be evaporated and recovered in the course of the process, which is fire hazard and
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und Umweltschutzprobleme mit sich bringen kann. Wenn das organische Lösungsmittel nicht wiedergewonnen wird, gestaltet sich das Überzugsverfahren unwirtschaftlich.and can cause environmental problems. If the organic solvent is not recovered, designed the coating process becomes uneconomical.
Es ist auch bekannt, die Fliessbettechnik für das Überziehen verschiedener,in Wasser löslicher oder dispergierbarer Partikel anzuwenden, wobei wässrige Lösungen von filmbildenden, wasserlöslichen Überzugsagenzien zerstäubt werden· ein solches Verfahren ist in dem US-Patent No. 3 196 827 (Wurster) beschrieben. Bei dem bekannten Verfahren besteht die Schwierigkeit, eine Agglomeration der zu überziehenden Partikel zu vermeiden, so dass darauf hingewiesen wird, dass dieses Verfahren nur für Partikel mit einer Grosse von mehr als 30 mesh (>-0,6 mm) geeignet ist. Nach der in der vorerwähnten US-Patentschrift beschriebenen Methode ist es auch schwierig F dünne überzüge 2u erhalten.It is also known to use the fluidized bed technique for coating various water-soluble or dispersible particles, wherein aqueous solutions of film-forming, water-soluble coating agents are atomized. Such a method is described in US Pat. 3 196 827 (Wurster). The known method has the difficulty of avoiding agglomeration of the particles to be coated, so it is pointed out that this method is only suitable for particles with a size of more than 30 mesh (> -0.6 mm). According to the US patent, in the aforementioned method described it is also difficult to obtain thin coatings F 2u.
Es wurde nun ein Verfahren entwickelt, mit dem es möglich ist, mit einer wässrigen oder im wesentlichen wässrigen Flüssigkeit im Fliessbettverfahren ein Produkt zu überziehen, dessen Teilchen eine Grosse von weniger als etwa 1 mm besitzen, wobei die Partikel mit einem äusserst dünnen Überzug versehen werden können, ohne dass die Gefahr einer Agglomeration besteht.A method has now been developed with which it is possible to use an aqueous or essentially aqueous liquid to coat a product in the fluidized bed process, the particles of which have a size of less than about 1 mm, the Particles can be provided with an extremely thin coating without the risk of agglomeration.
Das erfindungsgemässe Verfahren zum überziehen von in Wasser löslichen oder in Wasser dispergierbaren Partikeln nach dem Fliessbettverfahren, wobei die zu überziehenden Partikel inThe inventive method for coating in water soluble or water-dispersible particles according to the fluidized bed process, the particles to be coated in
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den Fliessbettreaktor eingebracht werden, ist dadurch gekennzeichnet, dass eine Überzugsflüssigkeit, die hauptsächlich aus einer wässrigen oder im wesentlichen wässrigen Lösung oder Dispersion eines einen makromolekularen Film bildenden, in Wasser löslichen oder in Wasser dispergierbaren Überzugs-the fluidized bed reactor is introduced, is characterized by that a coating liquid consisting mainly of an aqueous or essentially aqueous solution or dispersion of a macromolecular film-forming, water-soluble or water-dispersible coating
besteht
agens/durch Zerstäubung eingebracht wird, wobei die relative Feuchtigkeit der Auslassluft unter 100 % und die maximale
Grosse der durch die Zerstäubung erhaltenen Tröpfchen der
Überzugsflüssigkeit nicht über der kleinsten Grosse der zu
überziehenden Partikel liegt.consists
agent / is introduced by atomization, the relative humidity of the outlet air being below 100 % and the maximum size of the droplets of the coating liquid obtained by the atomization not exceeding the smallest size of the particles to be coated.
Wenn die maximale Grosse der zerstäubten Tröpfchen der Überzugsflüssigkeit über der kleinsten Grosse der zu überziehenden Partikel liegt, findet eine Agglomeration statt.When the maximum size of the atomized droplets of the coating liquid is greater than the smallest size of the particles to be coated, agglomeration takes place.
Folglich kann bei Anwendung der Erfindung eine Agglomeration vermieden werden und es besteht die Möglichkeit, eine Überzugsschicht mit einer Stärke bis herab zu etwa 0,1-10 ,u, vorzugsweise bis herab zu 0,5-1 /ι aufzubringen, was ungefähr 1 % des trockenen Partikelgewichts entspricht. Bei einer vorgegebenen Dicke der aus dem Überzugsagens bestehenden Schicht ist eine umso grössere auf das Partikelgewicht berechnete Menge an Überzugsagens erforderlich, je kleiner die Partikelgrösse ist. Dies wird durch die nachfolgende Tabelle I veranschaulicht. Consequently, when using the invention, agglomeration can be avoided and there is the possibility of applying a coating layer with a thickness down to about 0.1-10 μm, preferably down to 0.5-1 / ι , which is about 1 % corresponds to the dry particle weight. With a given thickness of the layer consisting of the coating agent, the smaller the particle size, the greater the amount of coating agent, calculated on the basis of the particle weight, is required. This is illustrated by Table I below.
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Tabelle I
Menge des Überzugsagens in Gew./6 der zu überziehenden PartikelTable I.
Amount of the coating agent in weight / sixth of the particles to be coated
ALCALASE P ALCALASE MALCALASE P ALCALASE M
Dicke des Über- mittlerer Teilchen- mittlerer Teilchenzugs durchmesser 400 ,u durchmesser 700 λχ Thickness of the over- mean particle- mean particle train diameter 400, u diameter 700 λχ
0,5 ya 0,8 % 0,5 % 0.5 ya 0.8 % 0.5 %
1,0 /U 1,5 % 0,9 % 1.0 / U 1.5 % 0.9 %
Wenngleich der nach der Erfindung erzeugte überzug vorzugsweise sehr dünn ist, so gestattet es die Erfindung jedoch auch. Überzüge mit einer Dicke von etwa 100 ai aufzubringen, falls dies aus irgendeinem Grunde gewünscht wird.Although the coating produced according to the invention is preferably very thin, the invention also allows it. Apply coatings approximately 100 ai thick if for any reason so desired.
Die kleinste Grosse der zu überziehenden Partikel kann durch . eine Siebanalyse ermittelt werden. Die maximale Grosse der durch Zerstäubung erhaltenen Tröpfchen der überzugsflussigkeit kann aus vom Düsenhersteller mitgelieferten Tabellen abgelesen werden, wenn die Viscosität der Flüssigkeit und der Druck bekannt ist.The smallest size of the particles to be coated can through. a sieve analysis can be determined. The maximum size of the through Spray obtained droplets of the coating liquid can can be read from the tables supplied by the nozzle manufacturer if the viscosity of the liquid and the pressure are known is.
Bei einer bevorzugten Ausführungsform der Erfindung enthalten die in Wasser loslichen oder in Wasser dispergierbaren Partikel, die überzogen werden sollen, ein oder mehrere Enzyme als Wirkstoff, beispielsweise Proteasen, Amylasen, Lipasen oder Cellulasen. Included in a preferred embodiment of the invention the water-soluble or water-dispersible particles, which are to be coated, one or more enzymes as an active ingredient, for example proteases, amylases, lipases or cellulases.
4098 86/13174098 86/1317
Bei einer anderen bevorzugten Ausführungsform bestehen das Enzym bzw. die Enzyme aus bakteriellen Proteinasen. Diese können erfindungsgemäss vorher mit einem Überzug versehen werden, um die Möglichkeit einer Staub- oder Abriebbildung zu reduzieren. Als bakterielle Proteinasen können erfindungsgemäss Alcalase P oder AIcalase M eingesetzt werden. Bei Alcalase (Warenzeichen der NOVO INDUSTRI A/S) handelt es sich um eine mikrobielle Proteinase. Alcalase P ist eine geprillte Alcalase. Alcalase M stellt eine Alcalase dar, die vermittelte eines Marumerizers behandelt wurde, wie es in der britischen Patentanmeldung No. 36 564/70 und in der französischen Patentschrift No. 2 099 349 beschrieben ist.In another preferred embodiment, they exist Enzyme or the enzymes from bacterial proteinases. According to the invention, these can be provided with a coating beforehand to reduce the possibility of dust or abrasion. According to the invention, as bacterial proteinases Alcalase P or Alcalase M can be used. at Alcalase (trademark of NOVO INDUSTRI A / S) is a microbial proteinase. Alcalase P is a prilled one Alcalase. Alcalase M represents an Alcalase that mediated of a marumerizer as described in British patent application no. 36 564/70 and in the French patent specification No. 2,099,349.
Für das erfindungsgemässe Verfahren können auch ein Enzym oder Enzyme eingesetzt werden, bei denen es sich um bakterielle oder fungale Carbohydrasen handelt.For the inventive method can also be an enzyme or Enzymes are used, which are bacterial or fungal carbohydrases.
Die erfindungsgemäss eingesetzten bakteriellen Amylasen können thermisch stabile Amylasen sein, die entsprechend dem britischen Patent No. 1 296 839 hergestellt wurden. The bacterial amylases used according to the invention can be thermally stable amylases which, according to British patent no. 1,296,839 were manufactured.
Für das erfindungsgemäss verwendete, einen makromolekularen Film bildende, wasserlösliche oder in Wasser dispergierbare Überzugsagens kann ein Cellulosederivat verwendet werden. Dabei kann dieses eine Methy!cellulose, Hydroxybutylmethylcellulose, Natriumcarboxymethylcellulose, Hydroxyäthylmethylcellulose oder eine Hydroxypropylmethylcellulose sein.For the macromolecular film-forming, water-soluble or water-dispersible used in the present invention A cellulose derivative can be used as the coating agent. This can be a methyl cellulose, hydroxybutylmethyl cellulose, Sodium carboxymethyl cellulose, hydroxyethyl methyl cellulose or a hydroxypropylmethyl cellulose.
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Bei einer anderen vorzugsweisen Ausführungsform des erfindungsgemässen Verfahrens wird für das einen makromolekularen Film bildende, in Wasser lösliche oder in Wasser dispergierende Überzugsagens ein Polyvinylpyrrolidon eingesetzt.In another preferred embodiment of the invention The procedure for this is a macromolecular film Forming, water-soluble or water-dispersing coating agent used a polyvinylpyrrolidone.
Das erfindungsgemässe Überzugsagens kann aber auch durch ein Polyäthylenglykol gebildet werden, das vorzugsweise ein Molekulargewicht zwischen etwa 400 und etwa 6000 besitzteThe coating agent according to the invention can, however, also be formed by a polyethylene glycol, which preferably has a molecular weight owned between about 400 and about 6000
Bei einer weiteren Ausführungsform der Erfindung besteht.das Überzugsagens aus einem Methacrylharz. Stattdessen kann aber auch Gelatine verwendet werden.In a further embodiment of the invention, there is Coating agent made from a methacrylic resin. Instead, you can gelatin can also be used.
Die Erfindung sieht vor, dass die Überzugsflüssigkeit ein Weichmachungsmittel enthalten kann. Zu diesem Zweck kann Glycerin verwendet werden. Dieses kann in einer Menge bis zu 60 %, vorzugsweise in einer Menge zwischen 10 und 30 %, bezogen auf das Trockengewicht des Überzugsagens,,eingesetzt werden.The invention provides that the coating liquid can contain a softening agent. Glycerin can be used for this purpose. This can be used in an amount of up to 60 %, preferably in an amount between 10 and 30 % , based on the dry weight of the coating agent.
Die Konzentration des den makromolekularen Film bildenden und in Wasser löslichen oder dispergierbaren Überzugsagens in der Uberzugsflüssigkext kann erfindungsgemäss zwischen 2 und 50 Gew.%, vorzugsweise zwischen 4 und 10 Gew.56 liegen.The concentration of the coating agent which forms the macromolecular film and is soluble or dispersible in water in the coating liquid can, according to the invention, be between 2 and 50% by weight , preferably between 4 and 10% by weight.
Bei Anwendung des erfindungsgemässen Verfahrens können die zu überziehenden Partikel einen mittleren Durchmesser zwischen 0,1 und 0,6 mm, vorzugsweise zwischen 0,2 und 0,6 mm aufweisen.When using the method according to the invention, the particles to be coated can have an average diameter between 0.1 and 0.6 mm, preferably between 0.2 and 0.6 mm.
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Die entsprechend dem erfindungsgemässen Verfahren erzeugte Überzugsschicht kann eine Stärke zwischen 0,1 und 10 ,u, vorzugsweise zwischen 0,5 und 1 ,u besitzen.The generated according to the inventive method Coating layer can have a thickness between 0.1 and 10 µ, preferably between 0.5 and 1, u have.
Das erfindungsgemässe Verfahren lässt sich entweder kontinuierlich oder chargenweise durchführen, wobei jedoch vorzugsweise letzteres der Fall ist. Dies gilt auch für die nachfolgenden Ausführungsbeispiele.The process according to the invention can either be carried out continuously or in batches, although the latter is preferably the case. This also applies to the following Embodiments.
Nach dem erfindungsgemässen Verfahren können in Wasser lösliche oder in Wasser dispergierbare Partikel gleich welcher Art eingesetzt werden, die aus irgendeinem Grunde mit einem Überzug versehen werden sollen. Lediglich als Beispiele dafür seien Enzymadditive wie proteolytische Enzymadditive für Detergent!-, en oder Arzneimittel in Kugelform oder oral anwendbare Penicillinaufbereitungen oder hygroscopische Substanzen wie Düngemittel genannt.In the process according to the invention, water-soluble or particles of any type which are dispersible in water are used to be coated for any reason. Just as examples Enzyme additives such as proteolytic enzyme additives for detergent! -, en or drugs in spherical form or orally applicable penicillin preparations or hygroscopic substances such as Called fertilizers.
Das Überziehen der Partikel kann aus verschiedenen Gründen erfolgen t beispielsweise um die Bildung von Abrieb zu vermindern, einen Schutz gegen Ultraviolettstrahlen, Feuchtigkeit oder Säureeinwirkung zu verleihen oder die Gefahr zu verringern, dass die Teilchen durch irgendeine Einwirkung verdorben werden.The particles can be coated for various reasons, for example to reduce the formation of abrasion, to provide protection against ultraviolet rays, moisture or the action of acids, or to reduce the risk that the particles will be spoiled by any action.
Nachfolgend sind einige Beispiele für das erfindungsgemäss zur Bildung eines makromolekularen Überzugsfilms verwendeter. in Wasser lösliche oder in Wasser dispergierbare'Überzugsagens angegeben: The following are some examples of the r used to form a macromolecular coating film in the present invention. Coating agents soluble or dispersible in water indicated:
40-9 8 86/ 1 3.1 740-9 8 86/1 3.1 7
METHOCEL ®MC 15: Methylcellulose mit einem Methoxyl SG (= Substitutionsgrad) von 1,64 bis 1,92 und einem PG (= Polymerisationsgrad) entsprechend einer Viscosität von 8 cP bis 10.000 cP in einer 2 &Lgen wässrigen Lösung bei 200C.METHOCEL ®MC 15: methyl cellulose having a methoxyl SG (= degree of substitution) from 1.64 to 1.92 and a PG (= degree of polymerization) corresponding to a viscosity of 8 cP to 10,000 cP in a 2 & lgen aqueous solution at 20 0 C.
TYLOSE^ C 10: Natriumcarboxymethylcellulose mit einem SG von 0,4 bis 1,5 und einem PG von 50 bis 1000.TYLOSE ^ C 10: Sodium carboxymethyl cellulose with a SG from 0.4 to 1.5 and a PG from 50 to 1000.
TYLOSE^MH 20: Methylhydroxyäthylcellulose (oder Hydroxyäthylmethylcellulose) mit einem Methoxyl SG von 1,0 bis 2,0, einem Hydroxyäthyl SG von 0,1 bis 0,5 und einem PG von 50 bis 1000.TYLOSE ^ MH 20: methyl hydroxyethyl cellulose (or hydroxyethyl methyl cellulose) with a methoxyl SG from 1.0 to 2.0, a hydroxyethyl SG from 0.1 to 0.5 and a PG from 50 to 1000.
METHOCEL V XD 1181: Hydroxypropylmethylcellulose mit einem Methoxyl SG von 1,0 bis 2,0, einem Hydroxypropyl SG von 0,1 bis 0,5 und einem PG von 50 bis 1000.METHOCEL V XD 1181: Hydroxypropylmethylcellulose with a Methoxyl SG from 1.0 to 2.0, a hydroxypropyl SG from 0.1 up to 0.5 and a PG from 50 to 1000.
KOLLIDON® K 25 PVP:. Polyvinylpyrrolidon mit einem durchschnittlichen Molekulargewicht von 10.000, 40.000, 160.000 und 360.000 und Mischungen davon, die ein zwischen diesen Werten liegendes durchschnittliches Molekulargewicht ergeben, sowie Mischungen oder einzelne Komponenten, die mit einem Weich» macher wie beispielsweise CMC und Celluloseazetat modifiziert sind.KOLLIDON® K 25 PVP :. Polyvinylpyrrolidone with an average molecular weight of 10,000, 40,000, 160,000 and 360,000 and mixtures thereof giving an average molecular weight intermediate these values, as well as Mixtures or individual components with a soft » Makers such as CMC and cellulose acetate are modified.
CARBOWAX ®: Polyäthylenglykole mit durchschnittlichen Mole kulargewichten von 400, 600, 1000, 1540, 4000, 6000 und Mischungen davon mit einem zwischen diesen Werten liegendenCARBOWAX ®: Polyethylene glycols with average moles Cell weights of 400, 600, 1000, 1540, 4000, 6000 and mixtures thereof with anything between these values
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durchschnittlichen Molekulargewicht.average molecular weight.
EUDEAGIT w. E 30 D: Methacrylharze und wässrige Dispersionen hiervon. Dieser Tablettenlack ist in alkalischen Flüssigkeiten völlig unlöslich.EUDEAGIT w . E 30 D: methacrylic resins and aqueous dispersions thereof. This tablet coating is completely insoluble in alkaline liquids.
SOLUGEL® : Gelatine»
Polypropylenglycole«,
Polyvinylalkohole.
Alginate«SOLUGEL®: gelatine »
Polypropylene glycols ",
Polyvinyl alcohols.
Alginates "
inin
Die Konzentration des Überzugsagens/der wässrigen oder im wesentlichen wässrigen Lösung oder Dispersion entspricht einer Viscosität, die eine Zerstäubung zulässt. Wie bereits erwähnt, kann die Konzentration zwischen 2 und 50 Gew.%, vorzugsweise zwischen 4 und 10 Gew.% liegen. Die Grenzen hängen jedoch weitgehend von dem jeweils eingesetzten Überzugsagens ab. Der durchschnittliche Durchmesser der zu überziehenden Teilchen liegt normalerweise zwischen 100 ,u und 600 bis 1000 ,u, vorzugsweise zwischen 200 ,u und 600 ,u. Die relative Feuchtigkeit in der Auslassluft sollte normalerweise nicht über 60 % liegen. Die Lufttemperatur, bei der die zu überziehenden Partikel in den Fliesszustand gebracht wird, sollte in Abhängigkeit von den Eigenschaften der zu überziehenden Partikel gewählt werden.The concentration of the coating agent / the aqueous or essentially aqueous solution or dispersion corresponds to a viscosity which allows atomization. As already mentioned, the concentration between 2 and 50 wt.%, Preferably between 4 and 10 wt.%. However, the limits largely depend on the particular coating agent used. The average diameter of the particles to be coated is normally between 100µ and 600 to 1000µ, preferably between 200µ and 600µ. The relative humidity in the exhaust air should normally not exceed 60 % . The air temperature at which the particles to be coated are brought into the flow state should be selected depending on the properties of the particles to be coated.
Die Qualität des Überzugs wird durch die Form der Partikel nicht beeinflusst. Nach der Erfindung ist es möglich, einenThe quality of the coating is not influenced by the shape of the particles. According to the invention it is possible to have a
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vollkommenen Überzug auf Kügelchen ebenso wie auf unregelmässig geformten Partikeln zu erzeugen. Einige der bekannten Überzugsverfahren sind nicht besonders gut für das überziehen von unregelmässig geformten Partikeln geeignet. In diesen Fällen wird nur ein unvollkommener überzug erreicht« Deshalb bringt das erfindungsgemässe Verfahren im Zusammenhang mit dem Überziehen von unregelmässig geformten Partikeln besondere Vorteile mit sich. Ein Beispiel für derartige unregelmässig geformte Partikel ist ein geprilltes Enzymprodukt, das geprillte Alcalase oder Alcalase P enthält. Wenn geprillte Alcalase entsprechend der Erfindung überzogen wird, ergibt sich ein Produkt, das aus unregelmässig geformten Partikeln besteht, die einen perfekten Überzug besitzen. Zufolge der unregelmässigen Form dieser Partikel wird deren Neigung, sich von den anderen Teilchen des in Pulverform vorliegenden Detergenz abzusondern, stark verringert. ' ■ ■"perfect coverage on globules as well as on irregular to produce shaped particles. Some of the known coating processes are not particularly good for coating irregularly shaped particles suitable. In these cases only an imperfect coating is achieved the method according to the invention in connection with the coating irregularly shaped particles with particular advantages. An example of such irregularly shaped Particle is a prilled enzyme product, prilled alcalase or Alcalase P contains. When prilled Alcalase is coated according to the invention, a product results which consists of irregularly shaped particles that have a perfect coating. Due to the irregular shape this particle becomes their tendency to separate from the other particles of the powder detergent, greatly reduced. '■ ■ "
Ein Additiv, das aus kugeligen. Teilchen besteht, die eine gegenüber den anderen Partikeln eines pulverförmigen Detergenz unterschiedliche Dichte aufweisen, besitzt eine solche Neigung, sich von den anderen Partikeln zu separieren, was zu einem inhomogenen Detergenz führt. Die vorerwähnten unregelraässig geformten Teilchen bieten deshalb für diesen Zweck besondere Vorteile.An additive made from spherical. Particle that consists of a have different densities compared to the other particles of a powdered detergent, has such a tendency to separate from the other particles, resulting in an inhomogeneous detergent. The aforementioned irregular shaped particles therefore offer particular advantages for this purpose.
Erfindungsgemäss kann die Überzugsflüssigkeit eine Weichmachersubstanz wie beispielsweise Triacetin enthalten, so wie esAccording to the invention, the coating liquid can be a plasticizer substance such as triacetin, just like it
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in dem nachfolgenden Beispiel 2 der Fall ist.is the case in Example 2 below.
Bei Verwendung von Glycerin als Weichmacher in der Uberzugsflussigkeit können überzogene Teilchen mit besonders günstigen Abriebwerten erhalten werden.When using glycerine as a plasticizer in the coating liquid Coated particles with particularly favorable abrasion values can be obtained.
Wird das Glycerin der Uberzugsflussigkeit in einer Menge bis zu 60 % des Trockengewichts des Überzugsagens oder so viel ah Glycerin zugesetzt, dass die überzogenen Partikel beginnen, aneinanderzukleben, vorzugsweise in einer Menge zwischen 10 und 30 % des Trockengewichts des Überzugsagens, wird der Abriebwert der überzogenen Partikel, wie sich aus der nachfolgenden Beschreibung ergibt, wesentlich verringert.If the glycerin is added to the coating liquid in an amount of up to 60 % of the dry weight of the coating agent or so much as glycerin that the coated particles begin to stick together, preferably in an amount between 10 and 30 % of the dry weight of the coating agent, the abrasion value of the coated Particles, as can be seen from the following description, are significantly reduced.
Zum besseren Verständnis dafür, in welcher Beziehung die verschiedenen Parameter des Verfahrens zu stehen haben, um eine relative Feuchtigkeit in der Auslassluft von weniger als 100 % zu erhalten, wird unter Bezugnahme auf Beispiel 21 die folgende Berechnung angestellt. Die Einlassluft, bei der es sich um die Luft in der Anlage handelte, besass folgende Werte:In order to better understand the relationship between the various parameters of the process in order to obtain a relative humidity in the outlet air of less than 100 % , the following calculation is made with reference to Example 21. The inlet air, which was the air in the system, had the following values:
Temperatur: 200C.Temperature: 20 0 C.
Relative Feuchtigkeit: 50 %entsprechend 7g H2O/kg Luft.Relative humidity: 50 % corresponding to 7g H 2 O / kg air.
Der Durchsatz der Überzugsflüssigkeit betrug 1700 ml/min· ader 102 l/h. Die Überzugsflüssigkeit hatte ein spezifischesThe throughput of the coating liquid was 1700 ml / min vein 102 l / h. The coating liquid had a specific one
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Gewicht von 1,0 g/cm und enthielt 10 Gew.£ an Überzugsagens, so dass die mit der Einführung der Uberzugsflüssigkeit verbundene Wasserzugabe bei 91,8 kg/h lag.Weight of 1.0 g / cm and contained 10 pounds by weight of coating agent, so that the addition of water associated with the introduction of the coating liquid was 91.8 kg / h.
Die Luft zur Erzeugung des Fliesszustandes wurde in einer Menge von 8000 N m /h oder 9600 kg/h durchgesetzt. Demnach wurden hiermit 0,007 χ 9600 = 67,2 kg Wasser in das System eingeführt. Dies ergibt pro Stunde eine Gesamtmenge von 91,8 + 67,2 kg Wasser, die in das System eingeführt wurde» Dies entspricht 159,0 kg Wasser, das zusammen mit etwa 9600 kg Luft aus dem System abgezogen wurde. Da die Auslassluft eine Temperatur von zwischen 23 und 27 C besass, entspricht diese Feuchtigkeitsmenge in der Auslassluft einer relativen Feuchtigkeit in der Auslassluft zwischen 95 und 75 %. Dies liegt im Rahmen der erfindungsgemässen Lehre. .The air for creating the flow state was passed through in an amount of 8000 Nm / h or 9600 kg / h. According to this, 0.007 χ 9600 = 67.2 kg of water was introduced into the system. This gives a total of 91.8 + 67.2 kg of water per hour that was introduced into the system »This corresponds to 159.0 kg of water that was withdrawn from the system together with about 9600 kg of air. Since the outlet air had a temperature of between 23 and 27 C, this amount of moisture in the outlet air corresponds to a relative humidity in the outlet air between 95 and 75 %. This is within the scope of the teaching according to the invention. .
Die Erfindung wird durch die nachfolgenden Beispiele weiter veranschaulicht. Die Beispiele 1 bis 10 beschreiben die Herstellung der Uberzugsflüssigkeit.The invention is further illustrated by the following examples. Examples 1 to 10 describe the preparation the coating liquid.
Methylcellulose (METHOCEL® MC 15) 50g Deionisiertes Wasser 1000 gMethyl cellulose (METHOCEL® MC 15) 50g Deionized water 1000 g
Die Methylcellulose wird mit etwa 333 g kochendem Wasser angerieben, wonach der Rest des Wassers (zweckmässigerweise kalt)The methyl cellulose is rubbed with about 333 g of boiling water, after which the rest of the water (preferably cold)
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■ - 13 -■ - 13 -
!unter Umrühren zugegeben wird. Die Lösung wird an einem kalten Ort stehen gelassen.! is added while stirring. The solution is left in a cold place.
Methylcellulose (METHOCEL ® MC 15) 50 gMethyl cellulose (METHOCEL ® MC 15) 50 g
Deionisiertes Wasser 1000 gDeionized water 1000 g
Triacetin 5 gTriacetin 5 g
Eine Lösung aus Methylcellulose und deionisiertem Wasser wird wie in.Beispiel 1 beschrieben hergestellt, wonach das Triacetin zugegeben wird,A solution of methyl cellulose and deionized water is prepared as described in Example 1, after which the triacetin is admitted
Natriumcarboxymethylcellulos'e (TYLOSE ^C 10) 50 g Deionisiertes Wasser 1000 gSodium carboxymethyl celluloses (TYLOSE ^ C 10) 50 g Deionized water 1000 g
Die Natriumcarboxymethylcellulose wird unter Umrühren unter Verwendung eines mit hoher Geschwindigkeit laufenden Mischers in Wasser aufgelöst.The sodium carboxymethyl cellulose is mixed with stirring using a high speed mixer dissolved in water.
Natriumcarboxylmethylcellulose (TYLOSE^C 10) 100 g Deionisiertes Wasser 1000 gSodium carboxylmethyl cellulose (TYLOSE ^ C 10) 100 g Deionized water 1000 g
Die Natriumcarboxylmethylcellulose wird unter Umrühren und Verwendung eines mit hoher Geschwindigkeit laufenden Mischers in Wasser aufgelöst.The sodium carboxymethyl cellulose is mixed with stirring using a high speed mixer dissolved in water.
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Methylhydroxylathylcellulose (TYLOSE®MH 20) 50 g Deionisiertes Wasser 1000 gMethylhydroxylethyl cellulose (TYLOSE®MH 20) 50 g Deionized water 1000 g
Die Methylhydroxylmethylcellulose wird unter Umrühren und Einsatzes einer mit hoher Geschwindigkeit laufenden Mischers in Wasser aufgelöst.The Methylhydroxylmethylcellulose is with stirring and Using a mixer running at high speed, dissolved in water.
Hydroxypropylmethylcellulose (METHOCEL® XD 1181) 50 g Deionisiertes Wasser 1000 gHydroxypropyl methyl cellulose (METHOCEL® XD 1181) 50 g Deionized water 1000 g
Die Hydroxypropylmethylcellulose wird unter Verwendung eines mit hoher Geschwindigkeit laufenden Mischers unter Umrühren in Wasser aufgelöst.The hydroxypropyl methyl cellulose is mixed using a high speed mixer with stirring dissolved in water.
Gelatine (SOLUGEL ®) 50 gGelatin (SOLUGEL®) 50 g
Deionisiertes Wasser 1000 gDeionized water 1000 g
Die Gelatine wird in Wasser unter Umrühren und unter Verwen-.dung eines schnell laufenden Mischers aufgelöst.The gelatin is poured into water while stirring and using of a fast-running mixer.
Polyvinylpyrrolidon (KOLLIDON® K 25) 50 gPolyvinylpyrrolidone (KOLLIDON® K 25) 50 g
Deionisiertes Wasser 1000 gDeionized water 1000 g
Das Polyvinylpyrrolidon wird in Wasser unter Umrühren mit einem schnell laufenden Mischer aufgelöst.The polyvinylpyrrolidone is added to water while stirring dissolved in a fast-running mixer.
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C-R)
Polyathylenglycol (CARBOWAX v^ 4000) ' 50 g CR)
Polyethylene glycol (CARBOWAX v ^ 4000) '50 g
Deionisiertes Wasser 1000 gDeionized water 1000 g
Das-Polyathylenglycol wird in Wasser unter Umrühren mit einem schnell laufenden Mischer aufgelöst.The polyethylene glycol is dissolved in water while stirring with a fast running mixer dissolved.
Polyathylenglycol (CARBOWAX® 6000) 50gPolyethylene glycol (CARBOWAX® 6000) 50g
Deionisiertes Wasser 1000 gDeionized water 1000 g
Das Polyathylenglycol wird in Wasser unter Umrühren mit einem schnell laufenden Mischer aufgelöst.The polyethylene glycol is dissolved in water while stirring with a high-speed mixer.
Die nach den vorstehenden Beispielen 1 bis 10 hergestellten Lösungen werden für das Überziehen von geprillter Alcalase (Alcalase P) in vier verschiedenen Fliessbettsystemen, die in den nachfolgenden Beispielen 11 bis 14beschrieben sind, eingesetzt.The solutions prepared according to Examples 1 to 10 above are used for coating prilled Alcalase (Alcalase P) in four different fluidized bed systems, which are described in Examples 11 to 14 below, used.
Anlage: "STREBA-I" (Aerometic AG, Basel)Annex: "STREBA-I" (Aerometic AG, Basel)
ALCALASE P: 1000 g Düse ALCALASE P: 1000 g nozzle
Druck 2 1/2 atoPressure 2 1/2 ato
Innendurchmesser 0,8 mmInner diameter 0.8 mm
Einlasstemperatur der Pliess-Inlet temperature of the Pliess
bettluft ■ ". 41°-43°Cbed air ■ ". 41 ° -43 ° C
409 8Ö6/ 1 31 7409 8Ö6 / 1 31 7
Temperatur der zu überziehendenTemperature of the to be coated
Teilchen 31° - 33°CParticles 31 ° - 33 ° C
Durchsatzgeschwindigkeit, derThroughput speed, the
Überzugsflüssigkeit 6 1/2 ml/min.Coating liquid 6 1/2 ml / min.
Fliessbettluft 8-10 Skaleneinheiten.Fluidized bed air 8-10 scale units.
11 (W. Glatt, Haltingen) 11 (W. Glatt, Haltingen)
Anlage:System:
ALCALASE P:ALCALASE P:
MantelpositionCoat position
InnendurchmesserInside diameter
"ffSG-30" (W. Glatt, Haltingen) 45.000 g "ffSG-30" (W. Glatt, Haltingen) 45,000 g
0,3 6 ato. 1,8 mm0.3 6 ato. 1.8 mm
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Einlasstemperatur der Fliessbettluft Inlet temperature of the fluidized bed air
Temperatur der zu überziehenden TeilchenTemperature of the particles to be coated
Durchsatzgeschwindigkeit der tiberzugsflussigkeit FliessbettluftThroughput rate of the coating liquid fluidized bed air
42° - 45°C42 ° - 45 ° C
31° - 33°C31 ° - 33 ° C
187 ml/min. 5 Skaleneinheiten187 ml / min. 5 scale units
Anlage:
ALCALASE P:
Düse System:
ALCALASE P:
jet
Mantelposition
DruckCoat position
pressure
Innendurchmesser
Einlasstemperatur der Fliessbettluft Inside diameter
Inlet temperature of the fluidized bed air
Temperatur der zu überziehenden TeilchenTemperature of the particles to be coated
Durchsatzgeschwindigkeit der tiberzugsflüssigkeit Durchsatz der Fliessbettluft Flow rate of the coating liquid Flow rate of the fluidized bed air
"STREBA-60M (Aeromatic AG, Basel) 135 kg"STREBA-60 M (Aeromatic AG, Basel) 135 kg
1,0
6 ato.
2r3 mm1.0
6 ato.
2 r 3 mm
42° - 45°C 31° - 33°C42 ° - 45 ° C 31 ° - 33 ° C
325 ml/min. entsprechend der Position der Drossel325 ml / min. according to the position of the throttle
In allen Fällen wurde ein Teilchenmaterial mit bemerkenswert guten Eigenschaften erhalten.In all cases, a particulate material with remarkably good properties was obtained.
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In der nachfolgenden Tabelle II ist der Anteil der Überzugsschicht auf den Partikeln und der Anteil an Abrieb angegeben, der in einigen der überzogenen und nach den Beispielen 12 bis 14 erhaltenen Produkte vorliegt* "t In Table II below, the proportion of the coating layer on the particles and the amount of abrasion is shown, which in some of the coated and obtained according to Examples 12 to 14 Products present * "t
Beispiel Uberzugsflussig- Anteil der Überzugs- Anteil an Abrieb keit entsprechend schicht auf dem in /Ug/100 g des No. den Beispielen Ko0 überzogenen Produkt ProduktsExample of coating liquid proportion of the coating proportion of abrasion corresponding to the layer on the in / Ug / 100 g of No. the examples Ko 0 coated product
total Enzymetotal enzymes
11
1
1 % 1/2 %
1 %
1550
15th
1,63.4
1.6
Die Beispiele 15 bis 20 beschreiben die Herstellung von Überzugsflüssigkeiten mit und ohne Glycerinzusatz.Examples 15 to 20 describe the preparation of coating liquids with and without added glycerine.
40 9886/131740 9886/1317
Methylcellulose (METHOCEL ® MC 15) 50 gMethyl cellulose (METHOCEL ® MC 15) 50 g
Deionisiertes Wasser 950 gDeionized water 950 g
Die Methylcellulose wird mit etwa 333 g kochendem Wasser angerieben, wonach der Rest des Wassers (zweckmässigerweise kalt) unter Umrühren zugegeben wird. Die Lösung wird an einem kalten Platz stehengelassen.The methyl cellulose is rubbed with about 333 g of boiling water, after which the rest of the water (conveniently cold) is added with stirring. The solution will be on a cold one Left place.
Methylcellulose (METHOCEL® MC 15) 42,5 gMethyl cellulose (METHOCEL® MC 15) 42.5 g
Glycerin 7,5 gGlycerin 7.5 g
Deionisiertes Wasser 950,0 gDeionized water 950.0 g
Eine Lösung aus Methylcellulose und deionisiertem Wasser wird wie in Beispiel 15 angegeben hergestellt, wonach Glycerin zugegeben wird.A solution of methyl cellulose and deionized water will be like indicated in Example 15, after which glycerol is added.
"Beispiel 17 " Example 17
Natriumcarboxymethylcellulose (CELLOFAS ^ B 5) 100 g Deionisiertes Wasser 900 gSodium carboxymethyl cellulose (CELLOFAS ^ B 5) 100 g Deionized water 900 g
Die Natriumcarboxymethylcellulose wird mit etwa 333 g kochendem Wasser, angerieben, wonach der Rest des Wassers (zweckmässigerweise kalt) unter Umrühren zugegeben wird. Die Lösung wird an einem kalten Platz stehengelassen.The sodium carboxymethyl cellulose is rubbed with about 333 g of boiling water, after which the rest of the water (conveniently cold) is added while stirring. The solution is left in a cold place.
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Natriumcarboxymethylcellulose (CELLOFAS ^ B 5) 85 gSodium carboxymethyl cellulose (CELLOFAS ^ B 5) 85 g
Glycerin 15 gGlycerin 15 g
Deionisiertes Wasser 900 gDeionized water 900 g
Eine Lösung aus Natriumcarboxymethylcellulose und deionisiertem Wasser wird wie in Beispiel 17 beschrieben hergestellt, wonach das Glycerin zugegeben wird.A solution of sodium carboxymethyl cellulose and deionized water is prepared as described in Example 17, after which the glycerin is added.
Beispiel 19Example 19
j j . .— HS) 100 g y y . .— HS) 100 g
Deionisiertes Wasser 900 gDeionized water 900 g
"Eine Lösung von Natriumcarboxymethylcellulose und deionisiertem Wasser wird wie in Beispiel 17 beschrieben hergestellt."A solution of sodium carboxymethyl cellulose and deionized Water is prepared as described in Example 17.
Natriumcarboxymethylcellulose (CEKOL^ HS) 85 gSodium carboxymethyl cellulose (CEKOL ^ HS) 85 g
Glycerin 15 gGlycerin 15 g
Deionisiertes Wasser 900 gDeionized water 900 g
Eine Lösung von Natriumcarboxymethylcellulose und deionisiertes Wasser wird wie in Beispiel 17 beschrieben hergestellt, wonach das Glycerin zugegeben wird.A solution of sodium carboxymethyl cellulose and deionized water is prepared as described in Example 17, after which the glycerin is added.
Die nach den vorstehenden Beispielen 15 bis 20 hergestellten Lösungen werden für das Überziehen von ALCALASE M in einem Fliessbettsystem entsprechend dem nachfolgenden Beispiel verwendet.Those prepared according to Examples 15 to 20 above Solutions for coating ALCALASE M in a fluidized bed system according to the following example used.
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Anlage:
ALCALASE M:
Düse . ,'System:
ALCALASE M:
Nozzle . , '
Manteldurchmesser
DruckJacket diameter
pressure
Innendurchmesser
Einlasstemperatur der Fliessbettluft Inside diameter
Inlet temperature of the fluidized bed air
Temperatur der zu überziehenden TeilchenTemperature of the particles to be coated
Durchsatzgeschwindigkeit der Überzugsflüssigkeit FliessbettluftThroughput rate of the coating liquid, fluidized bed air
11WSG-300" (W. Glatt, Haltingen) 600 kg Sechs-Kopf Düse 6,0 mm 6,0 ato. 11 WSG-300 "(W. Glatt, Haltingen) 600 kg six-head nozzle 6.0 mm 6.0 ato.
1,2 mm1.2 mm
46° - 500C46 ° - 50 0 C
23° - 27°C23 ° - 27 ° C
1700 ml/min. 8000 N m3/h1700 ml / min. 8000 Nm 3 / h
In allen Fällen wurden Produkte erhalten,deren Teilchen bemerkenswert gute Eigenschaften besassen, insbesondere in bezug auf den Abriebswert.In all cases, products were obtained whose particles were remarkable possessed good properties, particularly with regard to the abrasion value.
Der Anteil an Abrieb, der in den nach Beispiel 21 hergestellten Produkten vorlag, ist in der folgenden Tabelle III angegeben.The proportion of abrasion which was present in the products prepared according to Example 21 is given in Table III below.
Beispiel Überzugsflüssig- Anteil der Überzugs- Anteil an AbriebExample coating liquid proportion of the coating proportion of abrasion
keit entsprechend schicht auf dem in ,ug/100 g des No. den Beispielen No. überzogenen Produkt Produktscorresponding layer on the in. ug / 100 g des No. Examples No. coated product product
total Enzyme total enzymes
Aus der vorstehenden Tabelle III ergibt sich, dass durch die Verwendung von Glycerin als Weichmachersubstanz in der Überzugsflüssigkeit eine bemerkenswerte Verbesserung hinsichtlich der Abriebswerte der überzogenen Teilchen erzielt wird.From the above Table III it can be seen that the use of glycerine as a plasticizer substance in the coating liquid a remarkable improvement in the abrasion values of the coated particles is achieved.
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Claims (24)
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 |
---|---|
DE2435008A1 true DE2435008A1 (en) | 1975-02-06 |
Family
ID=26247797
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
DE2435008A Ceased DE2435008A1 (en) | 1973-07-23 | 1974-07-20 | PROCESS FOR COVERING WATER-SOLUBLE OR DISPERSIBLE PARTICLES ACCORDING TO FLOW-BED TECHNOLOGY |
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 (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1987007292A1 (en) * | 1986-05-21 | 1987-12-03 | Novo Industri A/S | Coated detergent enzymes |
EP2204095A1 (en) | 2008-12-23 | 2010-07-07 | Basf Se | Mix crystal, method for their manufacture and application thereof in the production of baking goods |
DE102019200138A1 (en) | 2019-01-08 | 2020-07-09 | Beiersdorf Ag | Preparation with cellulose particles coated with vinylamine / N-vinylformamide copolymer |
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Publication number | Priority date | Publication date | Assignee | Title |
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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 |
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EP1660637A4 (en) | 2003-08-25 | 2009-10-21 | Novozymes Inc | Variants of glycoside hydrolases |
EP1673451B1 (en) | 2003-10-10 | 2010-12-15 | Novozymes A/S | Protease variants |
JP4880469B2 (en) | 2003-10-23 | 2012-02-22 | ノボザイムス アクティーゼルスカブ | Protease with improved stability in detergents |
ES2437198T3 (en) | 2003-10-28 | 2014-01-09 | Novozymes Inc. | Polypeptides with beta-glucosidase activity and isolated polynucleotides encoding the polypeptides |
JP5059412B2 (en) | 2004-01-06 | 2012-10-24 | ノボザイムス アクティーゼルスカブ | Alicyclobacillus sp. Polypeptide |
DK2305703T3 (en) | 2004-01-30 | 2014-06-16 | Novozymes Inc | Polypeptides with cellulolytic enhancing activity and polynucleotides encoding them |
CN102250861A (en) | 2004-02-13 | 2011-11-23 | 诺维信公司 | Protease variants |
US7148404B2 (en) | 2004-05-04 | 2006-12-12 | Novozymes A/S | Antimicrobial polypeptides |
BRPI0512341A (en) | 2004-06-21 | 2008-03-04 | Novozymes As | isolated polypeptide having protease activity, isolated nucleic acid sequence, nucleic acid construct, expression vector, recombinant host cell, transgenic plant or plant part, transgenic non-human animal, use of at least one protease, methods for producing a polypeptide, to improve the nutritional value of an animal feed and to treat protein, animal feed, and, animal feed additive |
DK1781790T3 (en) | 2004-07-05 | 2016-01-18 | Novozymes As | ALFA-amylase variants WITH CHANGED PROPERTIES |
WO2006032277A1 (en) | 2004-09-21 | 2006-03-30 | Novozymes A/S | Subtilases |
US7816115B2 (en) | 2004-09-21 | 2010-10-19 | Novozymes A/S | Subtilases |
EP1794297B1 (en) | 2004-09-21 | 2011-02-23 | Novozymes A/S | Subtilases |
CN102212510A (en) | 2004-09-30 | 2011-10-12 | 诺维信股份有限公司 | Polypeptides having lipase activity and polynucleotides encoding same |
CN101253263B (en) | 2005-04-27 | 2014-07-02 | 诺维信股份有限公司 | Polypeptides having endoglucanase activity and polynucleotides encoding same |
EP2385112B1 (en) | 2005-07-08 | 2016-11-30 | Novozymes A/S | Subtilase variants |
CN101243182B (en) | 2005-08-16 | 2014-08-06 | 诺维信公司 | Subtilases |
WO2007019859A2 (en) | 2005-08-16 | 2007-02-22 | Novozymes A/S | Polypeptides of strain bacillus sp. p203 |
EP1941023B1 (en) | 2005-09-30 | 2017-04-05 | Novozymes Inc. | Methods for enhancing the degradation or conversion of cellulosic material |
WO2007107573A1 (en) | 2006-03-22 | 2007-09-27 | Novozymes A/S | Use of polypeptides having antimicrobial activity |
US8546106B2 (en) | 2006-07-21 | 2013-10-01 | Novozymes, Inc. | Methods of increasing secretion of polypeptides having biological activity |
EP2097519A2 (en) | 2006-12-21 | 2009-09-09 | Danisco US, INC., Genencor Division | Compositions and uses for an alpha-amylase polypeptide of bacillus species 195 |
KR20100014954A (en) | 2007-03-09 | 2010-02-11 | 다니스코 유에스 인크. | 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 |
JP5520828B2 (en) | 2007-11-05 | 2014-06-11 | ダニスコ・ユーエス・インク | Bacillus sp. TS-23 alpha-amylase variants with altered characteristics |
CA2704555A1 (en) | 2007-11-05 | 2009-05-14 | Danisco Us Inc. | Alpha-amylase variants with altered properties |
RU2526516C2 (en) | 2008-02-04 | 2014-08-20 | ДАНИСКО ЮЭс ИНК. | Ts23 alpha-amylase versions with altered properties |
DK2297313T3 (en) | 2008-06-06 | 2015-06-08 | Danisco Us Inc | ALPHA AMYLASE VARIETIES OF BACILLUS SUBTILIS AND METHODS OF USING IT |
EP2698434A1 (en) | 2008-06-06 | 2014-02-19 | Danisco US Inc. | Uses of an alpha-amylase from Bacillus subtilis |
JP5599113B2 (en) | 2008-06-06 | 2014-10-01 | ダニスコ・ユーエス・インク | Saccharification enzyme composition and saccharification method thereof |
EP2623591B1 (en) | 2008-06-06 | 2016-08-24 | Danisco US Inc. | Geobacillus stearothermophilus alpha-amylase (AMYS) variants with improved properties |
WO2010036515A1 (en) | 2008-09-25 | 2010-04-01 | Danisco Us Inc. | Alpha-amylase blends and methods for using said blends |
ES2526867T3 (en) | 2008-11-20 | 2015-01-16 | Novozymes Inc. | Polypeptide having amylolytic enhancer activity and polynucleotides encoding it |
US7771983B2 (en) | 2008-12-04 | 2010-08-10 | Novozymos, 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 |
WO2010104675A1 (en) | 2009-03-10 | 2010-09-16 | Danisco Us Inc. | Bacillus megaterium strain dsm90-related alpha-amylases, and methods of use, thereof |
WO2010115028A2 (en) | 2009-04-01 | 2010-10-07 | Danisco Us Inc. | Cleaning system comprising an alpha-amylase and a protease |
CN102388131B (en) | 2009-04-08 | 2014-04-30 | 丹尼斯科美国公司 | Halomonas strain WDG195-related alpha-amylases, and methods of use thereof |
US8569581B2 (en) | 2009-09-17 | 2013-10-29 | Novozymes, Inc | Polypeptides having cellulolytic enhancing activity and polynucleotides encoding same |
CN102648277B (en) | 2009-09-25 | 2015-05-20 | 诺维信公司 | Use of protease variants |
BR112012006487A8 (en) | 2009-09-25 | 2018-04-24 | Novozymes As | precursor subtilisin variant, isolated polynucleotide, nucleic acid construct, expression vector, host cell, cleaning composition or detergent, and method for producing a variant |
EP2483295B1 (en) | 2009-09-29 | 2015-11-25 | Novozymes Inc. | Polypeptides having cellulolytic enhancing activity and polynucleotides encoding same |
WO2011041504A1 (en) | 2009-09-30 | 2011-04-07 | Novozymes, Inc. | Polypeptides derived from thermoascus crustaceus 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 |
DK3101127T3 (en) | 2010-01-04 | 2019-05-13 | Novozymes North America Inc | Alpha-amylase variants with improved stability |
US9045514B2 (en) | 2010-01-22 | 2015-06-02 | Dupont Nutrition Biosciences Aps | Methods for producing amino-substituted glycolipid compounds |
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 |
MX342388B (en) | 2010-02-10 | 2016-09-28 | Novozymes As | Variants and compositions comprising variants with high stability in presence of a chelating agent. |
US8815559B2 (en) | 2010-02-18 | 2014-08-26 | Danisco Us Inc. | Amylase from nesterenkonia and methods of use, thereof |
MX2013003236A (en) | 2010-09-30 | 2013-05-30 | Novozymes Inc | Variants of polypeptides having cellulolytic enhancing activity and polynucleotides encoding same. |
WO2012044836A1 (en) | 2010-09-30 | 2012-04-05 | Novozymes, Inc. | Variants of polypeptides having cellulolytic enhancing activity and polynucleotides encoding same |
MX2013004758A (en) | 2010-11-18 | 2013-06-28 | Novozymes Inc | Chimeric polypeptides having cellulolytic enhancing activity and polynucleotides encoding same. |
EP2675882A1 (en) | 2011-02-16 | 2013-12-25 | Novozymes A/S | Detergent compositions comprising m7 or m35 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 |
CN103476915A (en) | 2011-02-16 | 2013-12-25 | 诺维信公司 | Detergent compositions comprising metalloproteases |
MX2013007997A (en) | 2011-02-23 | 2013-08-21 | Novozymes Inc | Polypeptides having cellulolytic enhancing activity and polynucleotides encoding same. |
US9410136B2 (en) | 2011-03-31 | 2016-08-09 | Novozymes, Inc. | Methods for enhancing the degradation or conversion of cellulosic material |
BR112013025811A2 (en) | 2011-04-08 | 2016-11-29 | Danisco Us Inc | "composition and method for removing a lipid based stain from a surface" |
BR112013027463A2 (en) | 2011-04-29 | 2017-09-26 | Novozymes Inc | methods for degrading or converting, and for fermenting a cellulolysis material, for producing a fermentation product, and for cleaning or washing a hard surface or dirty laundry, and detergent composition |
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 |
DK3543333T3 (en) | 2011-06-30 | 2022-02-14 | Novozymes As | METHOD FOR SCREENING ALFA AMYLASES |
EP2551335A1 (en) | 2011-07-25 | 2013-01-30 | The Procter & Gamble Company | Enzyme stabilized liquid detergent composition |
JP2014531895A (en) | 2011-08-15 | 2014-12-04 | ノボザイムス アクティーゼルスカブ | Polypeptide having cellulase activity and polynucleotide encoding the same |
US20140295027A1 (en) | 2011-08-19 | 2014-10-02 | Novozymes A/S | Polypeptides Having Protease Activity |
ES2628190T3 (en) | 2011-09-22 | 2017-08-02 | Novozymes A/S | Polypeptides with protease activity and polynucleotides encoding them |
CA2852603A1 (en) | 2011-10-17 | 2013-04-25 | Novozymes A/S | Alpha-amylase variants and polynucleotides encoding same |
US9334485B2 (en) | 2011-10-17 | 2016-05-10 | Novozymes A/S | Alpha-amylase variants and polynucleotides encoding same |
EP3845641A1 (en) | 2011-10-28 | 2021-07-07 | Danisco US Inc. | Variant maltohexaose-forming alpha-amylase variants |
CN103958672A (en) | 2011-11-21 | 2014-07-30 | 诺维信股份有限公司 | GH61 polypeptide variants and polynucleotides encoding same |
CN107090445A (en) | 2011-11-25 | 2017-08-25 | 诺维信公司 | The polynucleotides of polypeptide and coding said polypeptide with lysozyme activity |
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 |
MX2014007446A (en) | 2011-12-20 | 2014-08-01 | Novozymes As | Subtilase variants and polynucleotides encoding same. |
EP2794866A1 (en) | 2011-12-22 | 2014-10-29 | Danisco US Inc. | Compositions and methods comprising a lipolytic enzyme variant |
EP2794867A1 (en) | 2011-12-22 | 2014-10-29 | Danisco US Inc. | Variant alpha-amylases and methods of use, thereof |
US10174301B2 (en) | 2011-12-28 | 2019-01-08 | Novozymes A/S | Methods for improving the nutritional value of the animal feed using a protease |
DK3382003T3 (en) | 2011-12-29 | 2021-09-06 | Novozymes As | DETERGENT COMPOSITIONS WITH LIPASE VARIANTS |
EP2807254B1 (en) | 2012-01-26 | 2017-08-02 | Novozymes A/S | Use of polypeptides having protease activity in animal feed and detergents |
ES2582608T3 (en) | 2012-02-17 | 2016-09-14 | Henkel Ag & Co. Kgaa | Detergent compositions comprising subthylase variants |
US10093911B2 (en) | 2012-02-17 | 2018-10-09 | Novozymes A/S | Subtilisin variants and polynucleotides encoding same |
EP2823026A1 (en) | 2012-03-07 | 2015-01-14 | Novozymes A/S | Detergent composition and substitution of optical brighteners in detergent compositions |
WO2013163590A2 (en) | 2012-04-27 | 2013-10-31 | Novozymes, Inc. | Gh61 polypeptide variants and polynucleotides encoding same |
US9458441B2 (en) | 2012-05-07 | 2016-10-04 | Novozymes A/S | Polypeptides having xanthan degrading activity and polynucleotides encoding same |
MX2014013402A (en) | 2012-05-11 | 2014-11-26 | Danisco Inc | Use of alpha-amylase from aspergillus clavatus 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 |
CA2874061A1 (en) | 2012-06-08 | 2014-01-09 | Danisco Us Inc. | Variant alpha amylases with enhanced activity on starch polymers |
WO2013189802A1 (en) | 2012-06-19 | 2013-12-27 | 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 |
AR092112A1 (en) | 2012-08-16 | 2015-03-25 | Danisco Us Inc | METHOD OF USING ASPERGILLUS CLAVATUS AND PULULANASE A-AMYLASE FOR SACARIFICATION |
CN104603265A (en) | 2012-08-22 | 2015-05-06 | 诺维信公司 | Detergent compositions comprising metalloproteases |
US20150203793A1 (en) | 2012-08-22 | 2015-07-23 | Novozymes A/S | Metalloprotease from Exiguobacterium |
MX357022B (en) | 2012-08-22 | 2018-06-25 | Novozymes As | Metalloproteases from alicyclobacillus sp. |
WO2014081622A1 (en) | 2012-11-20 | 2014-05-30 | Danisco Us Inc. | Amylase with maltogenic properties |
CA2893454C (en) | 2012-12-07 | 2022-04-19 | Novozymes A/S | Washing method for textiles |
EP2931872B1 (en) | 2012-12-11 | 2018-01-17 | Danisco US Inc. | Trichoderma reesei host cells expressing a glucoamylase from aspergillus fumigatus and methods of use thereof |
WO2014090940A1 (en) | 2012-12-14 | 2014-06-19 | Novozymes A/S | Removal of skin-derived body soils |
WO2014093125A1 (en) | 2012-12-14 | 2014-06-19 | Danisco Us Inc. | Method of using alpha-amylase from aspergillus fumigatus and isoamylase for saccharification |
EP2904105A1 (en) | 2012-12-20 | 2015-08-12 | Danisco US Inc. | Method of using alpha-amylase from aspergillus terreus and pullulanase for saccharification |
WO2014099523A1 (en) | 2012-12-21 | 2014-06-26 | Danisco Us Inc. | Alpha-amylase variants |
EP2934177B1 (en) | 2012-12-21 | 2017-10-25 | Novozymes A/S | Polypeptides having protease activiy and polynucleotides encoding same |
WO2014099525A1 (en) | 2012-12-21 | 2014-06-26 | Danisco Us Inc. | Paenibacillus curdlanolyticus amylase, and methods of use, thereof |
US9902946B2 (en) | 2013-01-03 | 2018-02-27 | Novozymes A/S | Alpha-amylase variants and polynucleotides encoding same |
CN105229147B (en) | 2013-03-11 | 2020-08-11 | 丹尼斯科美国公司 | Alpha-amylase combinatorial variants |
EP2970830B1 (en) | 2013-03-14 | 2017-12-13 | Novozymes A/S | Enzyme and inhibitor contained in water-soluble films |
EP2976416B1 (en) | 2013-03-21 | 2018-05-16 | Novozymes A/S | Polypeptides with lipase activity and polynucleotides encoding same |
BR112015028666B8 (en) | 2013-05-14 | 2022-08-09 | Novozymes As | DETERGENT COMPOSITION, METHOD FOR PRODUCING IT, METHOD FOR CLEANING AN OBJECT AND USES OF THE COMPOSITION |
EP2997143A1 (en) | 2013-05-17 | 2016-03-23 | Novozymes A/S | Polypeptides having alpha amylase activity |
CN114634921A (en) | 2013-06-06 | 2022-06-17 | 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 |
WO2014204596A1 (en) | 2013-06-17 | 2014-12-24 | Danisco Us Inc. | Alpha-amylase from bacillaceae family member |
WO2014207224A1 (en) | 2013-06-27 | 2014-12-31 | 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 |
KR20160029080A (en) | 2013-07-04 | 2016-03-14 | 노보자임스 에이/에스 | Polypeptides with xanthan lyase activity having anti-redeposition effect and polynucleotides encoding same |
WO2015004102A1 (en) | 2013-07-09 | 2015-01-15 | Novozymes A/S | Polypeptides with lipase activity and polynucleotides encoding same |
EP3696264B1 (en) | 2013-07-19 | 2023-06-28 | Danisco US Inc. | Compositions and methods comprising a lipolytic enzyme variant |
EP3309249B1 (en) | 2013-07-29 | 2019-09-18 | Novozymes A/S | Protease variants and polynucleotides encoding same |
EP3027748B1 (en) | 2013-07-29 | 2019-09-18 | 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 |
WO2015049370A1 (en) | 2013-10-03 | 2015-04-09 | Novozymes A/S | Detergent composition and use of detergent composition |
WO2015050724A1 (en) | 2013-10-03 | 2015-04-09 | Danisco Us Inc. | Alpha-amylases from a subset of exiguobacterium, and methods of use, thereof |
WO2015050723A1 (en) | 2013-10-03 | 2015-04-09 | Danisco Us Inc. | Alpha-amylases from exiguobacterium, and methods of use, thereof |
BR112016010551A2 (en) | 2013-11-20 | 2017-12-05 | Danisco Us Inc | alpha-amylase variants having reduced susceptibility to protease cleavage and methods 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 |
EP3083954B1 (en) | 2013-12-20 | 2018-09-26 | 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 |
CN106062271A (en) | 2014-03-05 | 2016-10-26 | 诺维信公司 | Compositions and methods for improving properties of cellulosic textile materials with xyloglucan endotransglycosylase |
EP3114219A1 (en) | 2014-03-05 | 2017-01-11 | Novozymes A/S | Compositions and methods for improving properties of non-cellulosic textile materials with xyloglucan endotransglycosylase |
EP3521434A1 (en) | 2014-03-12 | 2019-08-07 | Novozymes A/S | Polypeptides with lipase activity and polynucleotides encoding same |
WO2015150457A1 (en) | 2014-04-01 | 2015-10-08 | Novozymes A/S | Polypeptides having 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 |
DK3406697T3 (en) | 2014-04-11 | 2020-08-31 | Novozymes As | Detergent composition |
CN106715465B (en) | 2014-04-15 | 2021-10-08 | 诺维信公司 | Polypeptides having lipase activity and polynucleotides encoding same |
US10023852B2 (en) | 2014-05-27 | 2018-07-17 | Novozymes A/S | Lipase variants and polynucleotides encoding same |
EP3878957A1 (en) | 2014-05-27 | 2021-09-15 | Novozymes A/S | Methods for producing lipases |
US20170121695A1 (en) | 2014-06-12 | 2017-05-04 | Novozymes A/S | Alpha-amylase variants and polynucleotides encoding same |
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 |
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 |
US10626388B2 (en) | 2014-07-04 | 2020-04-21 | Novozymes A/S | Subtilase variants and polynucleotides encoding same |
CA2950380A1 (en) | 2014-07-04 | 2016-01-07 | 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 |
US10287562B2 (en) | 2014-11-20 | 2019-05-14 | Novoszymes A/S | Alicyclobacillus variants and polynucleotides encoding same |
MX2017006695A (en) | 2014-12-04 | 2017-08-21 | Novozymes As | Subtilase variants and polynucleotides encoding same. |
EP4067485A3 (en) | 2014-12-05 | 2023-01-04 | Novozymes A/S | Lipase variants and polynucleotides encoding same |
ES2763235T3 (en) | 2014-12-15 | 2020-05-27 | Henkel Ag & Co Kgaa | Detergent composition comprising subtilase variants |
US20180000076A1 (en) | 2014-12-16 | 2018-01-04 | Novozymes A/S | Polypeptides Having N-Acetyl Glucosamine Oxidase Activity |
EP3234093B1 (en) | 2014-12-19 | 2020-05-27 | Novozymes A/S | Protease variants and polynucleotides encoding same |
US11518987B2 (en) | 2014-12-19 | 2022-12-06 | Novozymes A/S | Protease variants and polynucleotides encoding same |
WO2016162556A1 (en) | 2015-04-10 | 2016-10-13 | Novozymes A/S | Laundry method, use of dnase and detergent composition |
WO2016162558A1 (en) | 2015-04-10 | 2016-10-13 | Novozymes A/S | Detergent composition |
US10336971B2 (en) | 2015-05-19 | 2019-07-02 | Novozymes A/S | Odor reduction |
CN108012543B (en) | 2015-06-16 | 2022-01-04 | 诺维信公司 | Polypeptides having lipase activity and polynucleotides encoding same |
EP3106508B1 (en) | 2015-06-18 | 2019-11-20 | Henkel AG & Co. KGaA | Detergent composition comprising subtilase variants |
EP3872175A1 (en) | 2015-06-18 | 2021-09-01 | Novozymes A/S | Subtilase variants and polynucleotides encoding same |
US20180171271A1 (en) | 2015-06-30 | 2018-06-21 | Novozymes A/S | Laundry detergent composition, method for washing and use of composition |
EP3317407B1 (en) | 2015-07-01 | 2021-05-19 | Novozymes A/S | Methods of reducing odor |
WO2017005816A1 (en) | 2015-07-06 | 2017-01-12 | Novozymes A/S | Lipase variants and polynucleotides encoding same |
EP3350323B1 (en) | 2015-09-17 | 2021-04-14 | Novozymes A/S | Polypeptides having xanthan degrading activity and polynucleotides encoding same |
ES2794837T3 (en) | 2015-09-17 | 2020-11-19 | Henkel Ag & Co Kgaa | Detergent Compositions Comprising Polypeptides Having Xanthan Degrading Activity |
EP3708660A3 (en) | 2015-10-07 | 2020-12-30 | Novozymes A/S | Polypeptides |
EP4324919A2 (en) | 2015-10-14 | 2024-02-21 | Novozymes A/S | Polypeptide variants |
US20180171318A1 (en) | 2015-10-14 | 2018-06-21 | Novozymes A/S | Polypeptides Having Protease Activity and Polynucleotides Encoding Same |
WO2016203064A2 (en) | 2015-10-28 | 2016-12-22 | 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 |
WO2017093318A1 (en) | 2015-12-01 | 2017-06-08 | Novozymes A/S | Methods for producing lipases |
WO2017100720A1 (en) | 2015-12-09 | 2017-06-15 | Danisco Us Inc. | Alpha-amylase combinatorial variants |
MX2018007485A (en) | 2015-12-30 | 2018-08-01 | Novozymes As | Enzyme variants and polynucleotides encoding the same. |
WO2017129754A1 (en) | 2016-01-29 | 2017-08-03 | Novozymes A/S | Beta-glucanase variants and polynucleotides encoding same |
BR112018069220A2 (en) | 2016-03-23 | 2019-01-22 | Novozymes As | use of polypeptide that has dnase activity for tissue treatment |
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 |
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-
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 DK DK384574A patent/DK384574A/da not_active Application Discontinuation
- 1974-07-17 NL NL7409683A patent/NL7409683A/en 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 ES ES428475A patent/ES428475A1/en not_active Expired
- 1974-07-22 IT IT52219/74A patent/IT1016947B/en active
- 1974-07-23 AU AU71557/74A patent/AU498649B2/en not_active Expired
- 1974-07-23 AT AT606874A patent/AT357979B/en active
- 1974-07-23 FR FR7425523A patent/FR2238530B1/fr not_active Expired
- 1974-07-23 JP JP49084519A patent/JPS5071583A/ja active Pending
- 1974-07-23 IE IE1568/74A patent/IE41403B1/en unknown
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1987007292A1 (en) * | 1986-05-21 | 1987-12-03 | Novo Industri A/S | Coated detergent enzymes |
EP2204095A1 (en) | 2008-12-23 | 2010-07-07 | Basf Se | Mix crystal, method for their manufacture and application thereof in the production of baking goods |
US9894905B2 (en) | 2008-12-23 | 2018-02-20 | Basf Se | Mixed crystals, method for the production thereof and use thereof in the production of baked goods |
US10609931B2 (en) | 2008-12-23 | 2020-04-07 | Basf Se | Mixed crystals, method for the production thereof and use thereof in the production of baked goods |
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 |
Also Published As
Publication number | Publication date |
---|---|
AT357979B (en) | 1980-08-11 |
IE41403L (en) | 1975-01-23 |
FI219474A (en) | 1975-01-24 |
FR2238530A1 (en) | 1975-02-21 |
SE7409471L (en) | 1975-01-24 |
ES428475A1 (en) | 1976-12-16 |
CH604923A5 (en) | 1978-09-15 |
ATA606874A (en) | 1980-01-15 |
IT1016947B (en) | 1977-06-20 |
JPS5071583A (en) | 1975-06-13 |
NL7409683A (en) | 1975-01-27 |
IE41403B1 (en) | 1980-01-02 |
DK384574A (en) | 1975-03-03 |
AU7155774A (en) | 1976-01-29 |
BE817930A (en) | 1975-01-22 |
AU498649B2 (en) | 1979-03-22 |
GB1483591A (en) | 1977-08-24 |
FR2238530B1 (en) | 1979-03-09 |
CA1049334A (en) | 1979-02-27 |
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