EP0870007A1 - Enzyme granulate containing anti-corrosion agents for silver - Google Patents

Enzyme granulate containing anti-corrosion agents for silver

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Publication number
EP0870007A1
EP0870007A1 EP96920771A EP96920771A EP0870007A1 EP 0870007 A1 EP0870007 A1 EP 0870007A1 EP 96920771 A EP96920771 A EP 96920771A EP 96920771 A EP96920771 A EP 96920771A EP 0870007 A1 EP0870007 A1 EP 0870007A1
Authority
EP
European Patent Office
Prior art keywords
weight
enzyme
corrosion inhibitor
silver corrosion
silver
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.)
Withdrawn
Application number
EP96920771A
Other languages
German (de)
French (fr)
Inventor
Kathleen Paatz
Wilfried Rähse
Werner Pichler
Jürgen Härer
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Henkel AG and Co KGaA
Original Assignee
Henkel AG and Co KGaA
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Henkel AG and Co KGaA filed Critical Henkel AG and Co KGaA
Publication of EP0870007A1 publication Critical patent/EP0870007A1/en
Withdrawn legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11DDETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
    • C11D3/00Other compounding ingredients of detergent compositions covered in group C11D1/00
    • C11D3/02Inorganic compounds ; Elemental compounds
    • C11D3/04Water-soluble compounds
    • C11D3/046Salts
    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11DDETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
    • C11D3/00Other compounding ingredients of detergent compositions covered in group C11D1/00
    • C11D3/0005Other compounding ingredients characterised by their effect
    • C11D3/0073Anticorrosion compositions
    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11DDETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
    • C11D3/00Other compounding ingredients of detergent compositions covered in group C11D1/00
    • C11D3/16Organic compounds
    • C11D3/38Products with no well-defined composition, e.g. natural products
    • C11D3/386Preparations containing enzymes, e.g. protease or amylase
    • C11D3/38672Granulated or coated enzymes

Definitions

  • the invention relates to an enzyme granulate which contains a silver corrosion inhibitor, a process for its production and the use of the granulate in solid cleaning agents, in particular for machine dishwashing.
  • Enzymes are used extensively in detergents, washing aids and cleaning agents.
  • the enzymes are usually not used as concentrates, but in mixtures with a dilution and carrier material. If such enzyme preparations are admixed with conventional detergents or cleaning agents, a considerable reduction in the enzyme activity can occur during storage, especially if bleach-active compounds are present.
  • the storage stability of the enzymes can be significantly increased if the enzymes are encased or embedded in the carrier material and then converted into the desired particle shape by extrusion, pressing and marumerization, as described, for example, in German patent DE 16 17 232, German Offenlegungsschrift DT 20 32 768, and the German interpretations DE 21 37 042 and DE 21 37 043.
  • Such enzyme preparations only have poor solubility properties. The undissolved particles can get caught in the material to be cleaned and contaminate it, or they can be discharged into the waste water unused.
  • Embedding agents known from German patent specification DT 18 03 099 which consist of a mixture of solid acids or acidic salts and carbonates or bicarbonates and which disintegrate when water is added, improve the solvency, but are themselves very sensitive to moisture and therefore require additional protective measures.
  • enzyme granules for use in granular detergents and cleaning agents which contain 2% by weight to 20% by weight of enzyme, 10% by weight to 50% by weight of swellable starch, 5% by weight .-% to 50 wt .-% water-soluble organic polymer as Granuherellosxnittel, 10 wt .-% to 35 wt .-% cereal and 3 wt .-% to 12 wt .-% water.
  • Such an additive mixture enables enzyme processing without major loss of activity, and the storage stability of the enzymes in the granules is also satisfactory.
  • Silver can react when cleaning with sulfur-containing substances that are dissolved or dispersed in the rinsing water, because when cleaning dishes in household dishwashers, food residues and thus, among other things, mustard, peas, egg and other sulfur-containing compounds such as mercaptoamino acids are introduced into the washing liquor .
  • the much higher temperatures during machine rinsing and the longer contact times with the sulfur-containing food residues also favor the tarnishing of silver compared to manual rinsing. Due to the intensive cleaning process in the dishwashing
  • the silver surface is also completely degreased, making it more sensitive to chemical influences.
  • Such active oxygen bleaching agents are used, generally together with bleach activators, especially in modern, low-alkaline machine dishwashing detergents of the new generation of cleaners.
  • These agents generally consist of the following functional components: builder component (complexing agent dispersant), alkali carrier, bleaching system (combination of bleaching agent and bleach activator), enzyme and surfactant.
  • EP 135 226 and EP 135 227 describe weakly alkaline machine dishwashing detergents containing peroxy compounds and activators, which may contain benzotriazoles and fatty acids as silver preservatives. Finally, it is known from German published patent application DE 41 28 672 that peroxy compounds, which are activated by the addition of known organic bleach activators, prevent the tarnishing of silver parts in strongly alkaline cleaning agents.
  • German patent applications DE 43 25 922 and DE 43 15 397 describe the use of titanium, zirconium, hafnium, vanadium, cobalt or cerium salts and / or complexes in which the metals in one of the oxidation stages ⁇ , HL IV, V or VI are present, or of manganese (II) salts or complexes to prevent silver corrosion.
  • the international patent application WO 94/19445 describes the use of certain manganese (i ⁇ ) or manganese (TV) complexes as silver corrosion inhibitors in mechanical dishwashing detergents.
  • International patent application WO 94/07981 discloses the use of cysteine as a silver protection agent.
  • German patent application 195 18 693.1 describes the supercorrosion-inhibiting action of cystine, alone or in particular in combination with isocyanuric acid.
  • the unpublished German patent application DE 43 44 215 relates to enzyme granules suitable for incorporation into particulate cleaning agents in particular, containing enzyme and inorganic and / or organic carrier material in the core and optionally granulating aids onto which a uniform coating layer has been applied, which in particular applies a coating layer contains inorganic silver corrosion inhibitor.
  • These enzyme granules can be produced in particular by applying an aqueous solution or dispersion which contains the silver corrosion inhibitor to an enzyme-containing core.
  • Such a manufacturing process creates difficulties in the processing of water-insoluble or sparingly water-soluble silver corrosion inhibitors.
  • additional energy is required for the evaporation of the water applied with the silver corrosion inhibitor.
  • corrosion is to be interpreted in its broadest meaning in chemistry, in particular “corrosion” here should stand for any visually just recognizable change in a metal surface, here silver, be it for example a selective discoloration or be it for example large start-up.
  • this object is achieved by enzyme granulate containing silver corrosion inhibitor which is suitable for incorporation into particulate cleaning agents and which contains enzyme, inorganic and / or organic carrier material for the enzyme and silver corrosion inhibitor and optionally granulation aids in an intimate, so to say homogeneous mixture.
  • the organic silver corrosion inhibitors include compounds with a trivalent N atom, such as pyrazole, thionalide, morpholine, melamine, cysteine, 2-mercaptobenzodiazole, distearylamine, isocyanuric acid, bezotriazole, aminotriazole, aminotetrazole, indazole and imidazole and its derivatives, for example organic benzimidazole Disulfides, for example cystine, and di- and trihydric phenols and their derivatives, for example hydroquinone, pyrocatechol, phloroglucinol, gallic acid, hydroxyhydroquinone and pyrogallol.
  • a trivalent N atom such as pyrazole, thionalide, morpholine, melamine, cysteine, 2-mercaptobenzodiazole, distearylamine, isocyanuric acid, bezotriazole, aminotriazole, aminotetrazole, indazole and imid
  • inorganic silver corrosion inhibitors are manganese, titanium, zirconium, hafnium, vanadium, cobalt or cerium salts and / or complexes in which the metals mentioned are present in one of the oxidation states II, HI, IV, V or VI.
  • the counterions suitable for salt formation include all customary single, double or triple negatively charged inorganic anions, for example oxide, sulfate, nitrate, fluoride, but also organic anions such as stearate.
  • metal complexes are compounds which consist of a central atom and one or more ligands and, if appropriate, additionally one or more of the above-mentioned anions.
  • the central atom is one of the metals mentioned above in one of the oxidation states mentioned above. fen.
  • the ligands are neutral molecules or anions, which can be monodentate or multidentate; the term “ligand” in the sense of the invention is explained in more detail, for example, in “Römpp Chemie Lexikon, Georg Thieme Verlag Stuttgart / New York, 9th edition, 1990, page 2507”.
  • Preferred metal salts or metal complexes are MnSO 4 , V 2 O 5 , V 2 O 4 , VO 2 , TiOSO 4 , K 2 TiF 6 , K 2 ZrF 6 , CoSO 4 , Co (NO 3 ) 2 , Ce (NO 3 ) 3 as well as their mixtures.
  • salts or complexes are commercially available substances that can generally be used for the purpose of protecting against silver corrosion without prior cleaning.
  • the oxidic mixture of tetravalent and pentavalent vanadium (V 2 O 5 , VO 2 , V 2 O 4 ) known from SO 3 production (contact process) is suitable, as is that by diluting a Ti (SO) 2 - Solution with titanyl sulfate TiOSO 4 .
  • 0.5% by weight to 40% by weight in particular 1% by weight to 30% by weight and particularly preferably 2.5% by weight to 25% by weight, is preferably enzymatic Protein, 30% by weight to 95% by weight, in particular 40% by weight to 80% by weight of carrier material for the enzyme, optionally 3% by weight to 12% by weight of water and 0.5 % By weight to 50% by weight, in particular 5% by weight to 30% by weight, of silver corrosion inhibitor.
  • Enzymes primarily include the proteases, lipases, cutinases, amylases, pullulanases, hemicellulases, cellulases, oxidases and / or peroxidases obtained from microorganisms, such as bacteria or fungi, proteases produced by Bacillus species and their mixtures with amylases are preferred. They are obtained in a known manner by fermentation processes from suitable microorganisms, which are described, for example, in German patent applications DE 1940488, DE 2044 161, DE 22 01 803 and DE 21 21 397, US Pat. Nos. 3,632,957 and 4264 738 and European patent application EP 006638.
  • the method according to the invention for the formulation of very active proteases which are known, for example, from international patent application WO 91/02792 or US Pat. No. 5,340,735, are used because their storage-stable incorporation into detergents and cleaning agents often causes problems.
  • the enzyme granulate according to the invention is a protease-containing formulation
  • the protease activity is preferably 50,000 protease units (PE, determined by the method described in Tenside 7 (1970), 125) to 350,000 PE, in particular 100,000 PE up to 300,000 PE, per gram of enzyme granulate.
  • the particularly preferred enzyme granules according to the invention include those in which the enzyme protease and the silver corrosion inhibitor is MnSO, or in which the enzyme protease and the silver corrosion inhibitor is cystine, or in which the enzyme is amylase and the silver corrosion inhibitor cystine.
  • all organic or inorganic powdery substances which do not destroy or deactivate the enzymes to be granulated, or tolerably little, and which are stable under granulation conditions, can be used as carrier materials for the enzyme.
  • Such substances include, for example, starch, cereal flour, cellulose powder, alkali alumosilicate, in particular zeolite, layered silicate, for example bentonite or smectite, and water-soluble inorganic or organic salts, for example alkali metal chloride, alkali metal sulfate, alkali metal carbonate or alkali metal acetate, sodium or potassium being the preferred alkali metals.
  • a carrier material mixture of starch which is swellable in water, cereal flour and optionally cellulose powder and alkali carbonate is preferably used.
  • the starch which is swellable in water is preferably corn starch, rice starch, potato starch or mixtures thereof, the use of corn starch being particularly preferred.
  • Swellable starch is contained in the enzyme granules according to the invention preferably in amounts of from 20% by weight to 50% by weight, in particular from 25% by weight to 45% by weight.
  • the sum of the amounts of the swellable starch and the flour is preferably not more than 80% by weight, in particular 32% by weight to 65% by weight.
  • the cereal flour is in particular a product which can be produced from wheat, rye, barley or oats or a mixture of these flours, wholemeal flours being preferred.
  • a wholemeal flour is understood to mean a flour which has not been fully ground and which has been produced from whole, unpeeled grains or at least predominantly consists of such a product, the rest consisting of fully ground flour or starch.
  • Commercial wheat flour qualities such as type 450 or type 550 are preferably used. It is also possible to use flour products from the cereals leading to the aforementioned swellable starches, provided that care is taken to ensure that the flours have been produced from the whole grains.
  • the flour component of the additive mixture is known to achieve a substantial odor reduction in the enzyme preparation, which far exceeds the reduction in odor by incorporating the same amounts of corresponding starch types.
  • Such cereal flour is contained in the enzyme granules according to the invention preferably in amounts from 5% by weight to 35% by weight, in particular from 10% by weight to 25% by weight.
  • the enzyme granules according to the invention preferably contain, as a further component of the carrier material, 1% by weight to 50% by weight, preferably 5% by weight to 25% by weight, based on the total granulate, of a granulation aid system, the alkali carboxymethyl cellulose contains with degrees of substitution from 0.5 to 1 and polyethylene glycol and / or alkyl polyethoxylate.
  • This granulation aid system preferably contains, based in each case on finished enzyme granules, 0.5% by weight to 5% by weight of alkali carboxymethyl cellulose with degrees of substitution from 0.5 to 1 and up to 3% by weight of polyethylene glycol and / or Contain alkyl polyethoxylate, it being particularly preferred if at least 0.5% by weight, in particular 0.8% by weight to 2% by weight, of polyethylene glycol with an average molecular weight below 1000 and / or alkyl polyethoxylate with at least 30 ethoxy groups is present, if more than 2% by weight of alkali carboxymethyl cellulose is contained.
  • additional cellulose or starch ethers such as carboxymethyl starch, methyl cellulose, hydroxyethyl cellulose, hydroxypropyl cellulose and corresponding cellulose mixed ethers, gelatin, casein, tragacanth, maltodextrose, sucrose, invert sugar, glucose syrup or others can also be used as additional constituents of the granulation aid system
  • Water-soluble or readily dispersible oligomers or polymers of natural or synthetic origin can be used.
  • Usable synthetic water-soluble polymers are polyacrylates, polymethacrylates, copolymers of acrylic acid with maleic acid or compounds containing vinyl groups, furthermore polyvinyl alcohol, partially saponified polyvinyl acetate and polyvinyl pyrrolidone.
  • the aforementioned compounds are those with free carboxyl groups, they are normally in the form of their alkali metal salts, in particular their sodium salts.
  • Such additional granulation aids can be contained in the enzyme granules according to the invention in amounts of up to 10% by weight, in particular from 0.5% by weight to 8% by weight.
  • Higher molecular weight polyethylene glycols that is to say those with an average molecular weight of more than 1000, can be used as synthetic water-soluble polymers with a dust-binding effect, but it is precisely the higher molecular weight polyethylene glycols which cause an undesirable increase in the granule dissolution time required, so that these substances can be used in the invention
  • Enzyme granules are preferably completely absent.
  • the enzyme granules have a uniform outer coating layer.
  • a coating system which contains 10% by weight to 30% by weight of finely divided inorganic pigment, 45% by weight to 80% by weight of an alcohol or alcohol mixture with a melting point in the range of 35 ° C. is particularly suitable for the coating layer up to 75 ° C, up to 15 wt .-% emulsifier for the alcohol, up to 5 wt .-% dispersant for the pigment and up to 5 wt .-% water.
  • the alcohol component of the coating system is preferably a primary linear alcohol with 14 to 22 carbon atoms or a mixture of these.
  • the alcohols mentioned include in particular myristyl alcohol, cetyl alcohol, stearyl alcohol, arachidyl alcohol, behenyl alcohol and mono- to tri-unsaturated alcohols of appropriate chain length, it being essential that the alcohol component of the coating system mentioned has a melting point in the range from 35 ° C. to 75 ° C, in particular from 50 ° C to 60 ° C, which is to be understood here as the temperature at which 100% of the alcohol component is present in liquid form when heated.
  • Suitable emulsifiers for the alcohol component are substances which are able to emulsify the alcohol component in water so that a mixture which can be sprayed at temperatures of up to 95 ° C. is obtained and / or which allow the coating system to be as homogeneous as possible to transfer meltable sprayable at temperatures up to 120 ° C.
  • it can serve as a point of reference that liquids with viscosities of up to about 10,000 mPa.s can generally be sprayed without any problems at the temperatures mentioned by means of devices provided for this purpose and applied to enzyme granules.
  • the emulsifiers for the alcohol component of the coating system include, for example, the ethoxylation products of the alcohols mentioned, their reaction products with an average of 25 to 80, in particular 30 to 45, molar equivalents of ethylene oxide being preferred. If the coating system is applied to the enzyme granulate as an aqueous dispersion, preferred among the compounds mentioned are those with degrees of ethoxylation of 25 to 50, that is to say reaction products with 25 to 50 molar equivalents of ethylene oxide.
  • ethoxylated fatty acids the degree of ethoxylation preferably being 3 to 9, ethoxylated fatty acid amides, the degree of ethoxylation preferably being 4 to 11, and / or ethoxylation products of hydroxy fatty acid esters having 1 to 6 C- Atoms in the alcohol part of the ester, for example ricinoleic acid glyceride, where the degree of ethoxylation is preferably 5 to 80, in particular 20 to 40, can be used as the emulsifier component in the coating system.
  • the fatty acid component of the substances mentioned preferably has 12 to 22 carbon atoms. If desired, the ethoxy groups in the emulsifiers mentioned can be at least partially replaced by propoxy groups.
  • the inorganic pigments with which possible disruptive coloring of the enzyme granulate can be covered include, for example, calcium carbonate, Titanium dioxide, which can be in rutile or anatase crystal modification, zinc oxide, zinc sulfide, lead white (basic lead carbonate), barium sulfate, aluminum hydroxide, anti-monoxide, lithopone (zinc sulfide-barium sulfate), kaolin, chalk and / or mica. These are in such a finely divided form that they can be dispersed in a melt of the organic constituents of the coating system or in water.
  • the average particle size of such pigments is usually in the range from 0.004 ⁇ m to 50 ⁇ m.
  • this dispersion contains dispersing agents for the pigment and / or, as described below, the additional silver corrosion inhibitor which is optionally present in the coating system.
  • dispersants can be inorganic, for example aluminum oxide or silicon oxide, which can also serve as pigments, or organic, for example diethylene glycol or dipropylene glycol. Use with dispersants of surface-modified pigments is also possible.
  • Titanium dioxide pigment which is surface-modified with Al, Si, Zr or polyol compounds is preferred, in particular in rutile form, as is sold, for example, under the trade names Kronos® 2132 (Kronos-Titan) or Hombitan® R 522 (Sachtleben Chemie GmbH) , used.
  • the Tiona® RLL, AG and VC types from Solvay and the Bayertitan® RD, R-KB and AZ types from Bayer AG can also be used.
  • the coating system preferably has a content of at least 25% by weight of a silver corrosion inhibitor, in particular a silver corrosion inhibitor which is not identical to the silver corrosion inhibitor contained in the enzyme core, up to 30% by weight, in particular 5% by weight to 25% by weight.
  • % finely divided inorganic pigment 5% by weight to 75% by weight at room temperature solid alcohol with a melting point in the range from 35 ° C.
  • the enzyme granules containing silver corrosion inhibitor are preferably produced, at least in part, based on the processes of international patent application WO 92/11347 comprising an extrusion step or German patent application DE 43 10 506 using swellable starch, water-soluble organic polymer and cereal flour .
  • Another object of the invention thus relates to a method for producing an enzyme granulate containing silver corrosion inhibitor suitable for incorporation into particulate cleaning agents by mixing an aqueous liquid containing the enzyme, which liquid can optionally be a fermentation broth freed from insoluble constituents and concentrated. with inorganic and / or organic carrier material and the silver corrosion inhibitor, subsequent extrusion of the mixture obtained in this way through a perforated plate with subsequent cutting device, optionally spheronization of the extrudate in a rounding device and drying, and, if appropriate, application of a dye and / or pigment-containing coating, if desired train
  • Such a method has the advantage over known methods that it also makes it possible to process silver corrosion inhibitors which are insoluble or only slightly water-soluble.
  • the enzyme granules according to the invention are preferably prepared from fermentation broths which are freed of insoluble accompanying substances, for example by microfiltration.
  • the microfiltration is preferably carried out as a cross-flow microfiltration using porous tubes with micropores larger than 0.1 ⁇ m, flow rates of the concentrate solution of more than 2 m / s and a pressure difference to the permeate side of less than 5 bar, as for example in the European patent application EP 200 032.
  • the microfiltration permeate is then concentrated, preferably by ultrafiltration, if appropriate with subsequent vacuum evaporation.
  • the concentration can, as described in international patent application WO 92/11347, be carried out in such a way that only relatively low dry matter contents of preferably 5% by weight to 50% by weight, in particular 10% by weight up to 40% by weight.
  • the concentrate is expediently prepared beforehand in a dry, powdery to granular mixture of the additives described above. Impact substances, including the silver corrosion inhibitor, metered in and mixed in.
  • the water content of the mixture should be selected so that it can be converted into granular particles which do not stick at room temperature when processed with stirring and striking tools and plastically deformed and extruded when using higher pressures.
  • the free-flowing premix is, in principle, subsequently processed in a kneader and a connected extruder to form a plastic mass which is as homogeneous as possible Can heat 55 ° C.
  • the material leaving the extruder is passed through a perforated disk with a subsequent knock-off knife and is thereby reduced to cylindrical particles of a defined size.
  • the diameter of the bores in the perforated disk is expediently 0.7 mm to 1.6 mm, preferably 0.8 mm to 1.4 mm.
  • the particles in this form can then be dried and coated with a coating system.
  • a device which consists of a cylindrical container with stationary, fixed side walls and a friction plate rotatably mounted on the bottom.
  • Devices of this type are widely used in technology under the Marumerizer® product name and are described, for example, in the German specifications DE 21 37 042 and DE 21 37 043. Any dusty particles with a grain size of less than 0.1 mm, in particular less than 0.4 mm, and any coarse particles with a grain size of more than 2 mm, in particular more than 1.6 mm, can then be removed by sieving or air separation and, if necessary, in the Manufacturing process can be traced.
  • the beads can be added continuously or in batches, preferably using a fluidized bed drying unit, at supply air temperatures of preferably 35 ° C. to 50 ° C. and in particular at a product temperature of not more than 42 ° C. up to the desired residual moisture content of, for example, 4% by weight. % to 10% by weight, in particular 5% by weight to 8% by weight, based on the total granulate, are dried.
  • the coating system which optionally contains additional silver corrosion inhibitor, can be applied as an outer covering.
  • the coating system is in the form of an aqueous solution or dispersion which preferably contains 30% by weight to 65% by weight of water and 35% by weight to 70% by weight of the coating system, in particular 1 % By weight to 2.5% by weight, based on the entire coating system, of dispersant for the pigment and / or the silver corrosion inhibitor, is introduced into the fluidized bed of enzyme extrudate.
  • the water supplied via the aqueous dispersion is removed during the drying which is carried out simultaneously or is subsequently necessary again.
  • the coating system optionally with cooling, is applied to the enzyme-containing extrudate as a heated liquid at a temperature of 5 ° C. to 45 ° C.
  • a further embodiment of this method comprises the production of enzyme granules which contain two or more different enzymes.
  • the procedure is preferably such that an enzyme core containing super-anticorrosive agents, prepared as described by extrusion, is mixed with a second enzyme which has been made up in particulate form and, if appropriate, further enzymes made up in particulate form, under agglomeration conditions, a binder optionally being used, and the coating material is then used or applies simultaneously, the average particle size of the extrudate core containing the first enzyme preferably being 1.1 to 3 times, in particular 1.3 to 2 times that of the second or further enzyme-shaped enzyme.
  • This variant is based on the production method for multi-enzyme granules disclosed in German patent application DE 43 29463.
  • the enzyme in the extrudate core is preferably Protease and in the enzyme contained in the separately produced, smaller particles which agglomerate to the extrudate or in the enzymes, if several different smaller particles are used, to amylase, pullulanase, lipase, cutinase, hemicellulase, cellulase, peroxidase and / or Oxidase.
  • multi-enzyme granules containing silver corrosion inhibitor which contain protease in the extrudate core and amylase and / or lipase in the separately produced, smaller particles, are particularly preferred.
  • the enzyme preparation obtained by the process according to the invention consists of largely rounded, uniformly coated and dust-free particles which generally have a bulk density of approximately 500 to 900 grams per liter, in particular 650 to 880 grams per liter.
  • the granules according to the invention are notable for very high storage stability, in particular at temperatures above room temperature and high atmospheric humidity, and good dissolution behavior in the detergent liquor.
  • the enzyme granulate according to the invention or produced by the method according to the invention is preferably used for the production of solid, in particular particulate cleaning agents which can be obtained by simply mixing the enzyme granules with other powder components customary in such agents.
  • the enzyme granules preferably have average grain sizes in the range from 0.8 mm to 1.6 mm.
  • the granules according to the invention preferably contain less than 2% by weight, in particular at most 1.4% by weight, of particles with particle sizes outside the range from 0.4 mm to 1.6 mm.
  • a further subject of the invention is a lower-alkaline agent for machine cleaning of dishes whose 1% by weight solution has a pH of 8 to 11.5, preferably 9 to 10.5, containing enzyme, silver corrosion inhibitor, 15% by weight to 60% by weight, preferably 30% by weight to 50% by weight of water-soluble builder component, 5% by weight % up to 25% by weight, preferably 10% by weight to 15% by weight of oxygen-based bleach, 1% by weight to 10% by weight, preferably 2% by weight to 6% by weight of bleach activator, in each case based on the total agent, which is characterized in that it contains 0.1% by weight to 10% by weight, in particular 0.5% by weight to 5% by weight, of enzyme granules, which enzyme, inorganic and / or contains organic carrier material for the enzyme and silver corrosion protection agent and optionally granulation aids in intimate mixture.
  • organic disulfides dihydric phenols, trihydric phenols, manganese, titanium, zirconium, hafiiium, vanadium, cobalt or cerium salts and / or - complexes in which the metals mentioned are in one of the oxidation states ⁇ , IQ, IV, V or VI are present, preferred silver corrosion inhibitors.
  • all builders typically used in machine dishwashing detergents for example polymeric alkali metal phosphates, which can be present in the form of their alkaline neutral or acidic sodium or potassium salts, are suitable as water-soluble builder components in such low-alkaline cleaning agents.
  • examples of this are tetrasodium diphosphate, disodium dihydrogen diphosphate, pentasodium tri-phosphate, so-called sodium hexametaphosphate and the corresponding potassium salts or mixtures of sodium and potassium salts.
  • Their amounts can range up to about 35% by weight, based on the total agent; however, the agents according to the invention are preferably free of such phosphates.
  • water-soluble builder components are, for example, organic polymers of native or synthetic origin, especially polycarboxylates, which act as co-builders, in particular in hard water regions.
  • polyacrylic acids and copolymers of maleic anhydride and acrylic acid and the sodium salts of these polymer acids are suitable.
  • Commercial products are, for example, Sokalan® CP 5 and PA 30 from BASF.
  • Polymers of native origin that can be used as co-builders include, for example, oxidized starch, as known, for example, from international patent application WO 94/05762, and polyamino acids such as polyglutamic acid or polyaspartic acid.
  • hydroxycarboxylic acids such as, for example, mono-, dihydroxysuccinic acid, ⁇ -hydroxypropionic acid and gluconic acid.
  • the preferred builder components include the salts of the citro- Nenoic acid, especially sodium citrate.
  • Anhydrous trisodium citrate and preferably trisodium citrate dihydrate are suitable as sodium citrate. Trisodium citrate dihydrate can be used as a fine or coarse crystalline powder.
  • the acids corresponding to the co-builder salts mentioned can also be present.
  • Suitable oxygen-based bleaches are primarily sodium perborate mono- or tetrahydrate and / or sodium percarbonate.
  • the use of sodium percarbonate has advantages, since this has a particularly favorable effect on the corrosion behavior on glasses.
  • the oxygen-based bleach is therefore preferably a percarbonate salt, especially sodium percarbonate. Since bleaching agents based on oxygen generally only develop their full effect at elevated temperatures, so-called bleach activators are used to activate them at about 60 ° C. and below, that is to say the approximate temperatures of the cleaning process in the dishwasher.
  • Pentaacetylglucose, l, 5-diacetyl-2,2-dioxo-hexahydro-l, 3,5-triazine (DADHT) and / or isatoic anhydride can be used as bleach activators, but preferably N, N, N ', tetraacetylethylenediamine (TAED).
  • TAED tetraacetylethylenediamine
  • known peroxycarboxylic acids for example dodecanediperic acid or phthalimidopercarboxylic acids, which can optionally be substituted on the aromatic, can also be present.
  • bleach stabilizers such as, for example, phosphonates, borates or metaborates " and metasilicates and magnesium salts such as magnesium sulfate can also be useful.
  • the agents according to the invention preferably contain the alkali carriers, such as, for example, alkali silicates, alkali carbonates and / or alkali bicarbonates, contained in customary low-alkaline machine dishwashing detergents.
  • Alkali silicates can be used in amounts of up to 30% by weight .-%, based on the total agent, may be included.
  • the use of the highly alkaline metasilicates as alkali carriers is preferably avoided entirely.
  • the alkali carrier system preferably used in the agents according to the invention is a mixture of carbonate and bicarbonate, preferably sodium carbonate and bicarbonate, which is contained in an amount of up to 60% by weight, preferably 10% by weight to 40% by weight.
  • carbonate and bicarbonate preferably sodium carbonate and bicarbonate
  • the ratio of carbonate and hydrogen carbonate used varies, but an excess of sodium hydrogen carbonate is usually used, so that the weight ratio between hydrogen carbonate and carbonate is generally 1: 1 to 15: 1 is.
  • the agents according to the invention can contain ready-made enzymes such as proteases, amylases, lipases and cellulases which are not in the form of the granules according to the invention, for example proteases such as BLAP®, Optiase®, Opticlean®, Maxacal®, Maxapem®, Esperase ® and / or Savinase®, amylases like Termamyl®, Amylase-LT® and / or Maxamyl®, lipases like Lipolase®, Lipomax®, Lumafast® and / or Lipozym®, cellulases like Celluzym® and / or KAC®.
  • proteases such as BLAP®, Optiase®, Opticlean®, Maxacal®, Maxapem®, Esperase ® and / or Savinase®, amylases like Termamyl®, Amylase-LT® and / or Maxamyl®, lipa
  • surfactants in particular low-foaming nonionic surfactants, can also be added to the agents according to the invention, which serve to better detach fatty food residues, as wetting agents and, if appropriate, as granulating aids in the course of the preparation of the cleaning agents.
  • Their amount can be up to 5% by weight, preferably up to 2% by weight.
  • Extremely low-foaming compounds are usually used in particular in cleaning agents for use in machine dishwashing processes. These preferably include C 2 -C alkyl polyglycol-propylene glycol ether, each with up to 8 moles of ethylene oxide and propylene oxide units in the molecule.
  • C ⁇ -Cis-alkylpolyethylene glycol-polybutylene glycol ether each with up to 8 moles of ethylene oxide and butylene oxide units in the molecule
  • end-capped alkylpolyalkylene glycol mixed ethers and the foaming but ecologically attractive Cg- C H alkyl polyglucosides with a degree of polymerization of about 1 to 4 (eg APG® 225 and APG® 600 from Henkel) and / or C 2 -C 14 alkyl polyethyleneglycols with 3 to 8 ethylene oxide units in the molecule.
  • surfactants from the family of glucamides such as, for example, alkyl-N-methyl-glucamides, in which the alkyl part preferably comes from a fatty alcohol with the C chain length C ⁇ -Cu. It is sometimes advantageous if the surfactants described are used as mixtures den, for example the combination of alkyl polyglycoside with fatty alcohol ethoxylates or glucamide with alkyl polyglycosides.
  • the cleaning agents foam too much during use, they can still contain up to 6% by weight, preferably about 0.5% by weight to 4% by weight, of a foam-suppressing compound, preferably from the group of silicone oils, mixtures of silicone oil and hydrophobicized silica, paraffins, paraffin-alcohol combinations, hydrophobicized silica, the bisfatty acid amides, and other other known commercially available defoamers.
  • a foam-suppressing compound preferably from the group of silicone oils, mixtures of silicone oil and hydrophobicized silica, paraffins, paraffin-alcohol combinations, hydrophobicized silica, the bisfatty acid amides, and other other known commercially available defoamers.
  • Other optional ingredients in the agents according to the invention are, for example, perfume oils.
  • the dishwashing detergents according to the invention are preferably in the form of powdery, granular or tablet-like preparations which, in a manner known per se, for example by mixing, granulating, roller compacting and / or by spray drying the thermally loadable components and admixing the more sensitive components, to which in particular the enzyme granulate according to the invention is to be expected, can be produced.
  • the procedure is preferably such that all constituents are mixed with one another in a mixer and the mixture by means of conventional tablet presses, for example eccentric presses or rotary presses, with pressing pressures in the range from 200 • 10 5 Pa to 1 500 • 10 5 Pa pressed.
  • a tablet produced in this way preferably has a weight of 15 g to 40 g, in particular 20 g to 30 g, with a diameter from 35 mm to 40 mm.
  • Dishwashing detergents according to the invention in the form of non-dusting, storage-stable, free-flowing powders and / or granules with high bulk densities in the range from 800 to 1000 g / 1 can be carried out by adding the builder components with at least a proportion of liquid mixture components in a first process stage Increase in the bulk density of this premixed mixture and subsequently - if desired after an intermediate drying - the other constituents of the agent, including the enzyme granules containing silver corrosion inhibitor, combined with the premix obtained in this way.
  • the agents can be used both in household dishwashers and in commercial dishwashers. It is added by hand or using suitable dosing devices.
  • the application concentrations in the cleaning liquor are generally about 1 to 8 g / 1, preferably 2 to 5 g / 1.
  • a machine wash program is generally supplemented and ended by a few intermediate rinse cycles with clear water and a rinse cycle with a customary rinse aid after the cleaning cycle. After drying, when using the agents according to the invention, not only are completely clean dishes which are an from a hygienic point of view, but above all also bright silver cutlery items.
  • aqueous protease concentrate obtained after fermentation, removal of the fermentation residues by decanting, microfiltration in an ultrafiltration system and further concentration by means of vacuum evaporation as described in international patent application WO 91/02792 was mixed with the additives listed in the table below in a laboratory mixer from Lödige® homogeneously mixed and converted into granules with the aid of an extruder with a cutting device.
  • the hole diameter of the perforated plate of the extruder was 0.8 mm.
  • the ratio of length to thickness of the granules was 1.
  • the grain fraction between 0.4 mm and 1.6 mm was in a ball coater with Turbojet system from Wilsontlin with a coating layer coated, a melt of 70% by weight technical stearyl alcohol, 6% by weight 40 times ethoxylated tallow fatty alcohol and 24% by weight titanium dioxide being used.
  • the enzyme granulate containing silver protective agent obtained had a protease activity of 145,600 PE / g.

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Abstract

The aim is to develop a process by means for producing in the simplest possible way an enzyme-containing granulate suitable for incorporation in particulate cleaning agents which also contains anti-corrosion agents for silver, e.g. in the form of certain organic redox substances, in which said components, especially the enzyme, have a long shelf life. This has essentially been achieved by the preparation of a granulate containing an intimate mixture of the enzyme, an inorganic and/or organic vehicle therefor, and a silver corrosion inhibitor and possibly granulation auxiliaries. The enzyme granulates may be used to produce solid, especially particulate cleaning agents.

Description

" Silberkorrosionsschutzmittelhaltige Enzymgranulate" "Enzyme Granules Containing Silver Corrosion Protection Agents"
Die Erfindung betrifft ein Enzymgranulat, welches einen Silberkorrosionsinhibitor enthält, ein Verfahren zu seiner Herstellung und die Verwendung des Granulats in festen Reini¬ gungsmitteln, insbesondere zur maschinellen Geschirreinigung.The invention relates to an enzyme granulate which contains a silver corrosion inhibitor, a process for its production and the use of the granulate in solid cleaning agents, in particular for machine dishwashing.
Enzyme, insbesondere Proteasen, finden ausgedehnte Verwendung in Wasch-, Waschhilfs¬ und Reinigungsmitteln. Üblicherweise kommen die Enzyme dabei nicht als Konzentrate, sondern in Mischungen mit einem Verdünnungs- und Trägermaterial zum Einsatz. Mischt man solche Enzymzubereitungen üblichen Wasch- oder Reinigungsmitteln bei, so kann beim Lagern ein erheblicher Abbau der Enzymaktivität eintreten, insbesondere wenn bleichaktive Verbindungen zugegen sind. Das Aufbringen der Enzyme auf Trägersalze unter gleichzeitiger Granulation gemäß der deutschen Offenlegungsschrift DT 16 17 190 beziehungsweise durch Aufkleben mit nichtionischen Tensiden gemäß der deutschen Of¬ fenlegungsschrift DT 16 17 188 oder wäßrigen Lösungen von Celluloseethern gemäß der deutschen Offenlegungschrift DT 17 67 568 führt nicht zu einer nennenswerten Verbes¬ serung der Lagerstabilität, da sich die empfindlichen Enzyme in solchen Aufinischungen in der Regel auf der Oberfläche der Trägersubstanz befinden. Zwar kann die Lagerstabilität der Enzyme wesentlich erhöht werden, wenn man die Enzyme mit dem Trägermaterial umhüllt beziehungsweise in dieses einbettet und anschließend durch Extrudieren, Pressen und Marumerisieren in die gewünschte Partikelform überfuhrt, wie zum Beispiel in der deutschen Patentschrift DE 16 17 232, der deutschen Offenlegungsschrift DT 20 32 768, und den deutschen Auslegeschriften DE 21 37 042 und DE 21 37 043 beschrieben. Derar¬ tige Enzymzubereitungen besitzen jedoch nur mangelhafte Löslichkeitseigenschaften. Die ungelösten Partikel können sich im zu reinigenden Gut verfangen und dieses verunreinigen bzw. sie werden ungenutzt in das Abwasser überführt. Aus der deutschen Auslegeschrift DT 18 03 099 bekannte Einbettungsmittel, die aus einem Gemisch fester Säuren be¬ ziehungsweise saurer Salze und Carbonaten beziehungsweise Bicarbonaten bestehen und bei Wasserzusatz zerfallen, verbessern zwar das Lösungsvermögen, sind aber ihrerseits sehr empfindlich gegen Feuchtigkeit und erfordern daher zusätzliche Schutzmaßnahmen.Enzymes, especially proteases, are used extensively in detergents, washing aids and cleaning agents. The enzymes are usually not used as concentrates, but in mixtures with a dilution and carrier material. If such enzyme preparations are admixed with conventional detergents or cleaning agents, a considerable reduction in the enzyme activity can occur during storage, especially if bleach-active compounds are present. The application of the enzymes to carrier salts with simultaneous granulation according to German Offenlegungsschrift DT 16 17 190 or by sticking with nonionic surfactants according to German Offenlegungsschrift DT 16 17 188 or aqueous solutions of cellulose ethers according to German Offenlegungsschrift DT 17 67 568 does not lead to one significant improvement in storage stability, since the sensitive enzymes in such mixtures are generally on the surface of the carrier substance. The storage stability of the enzymes can be significantly increased if the enzymes are encased or embedded in the carrier material and then converted into the desired particle shape by extrusion, pressing and marumerization, as described, for example, in German patent DE 16 17 232, German Offenlegungsschrift DT 20 32 768, and the German interpretations DE 21 37 042 and DE 21 37 043. However, such enzyme preparations only have poor solubility properties. The undissolved particles can get caught in the material to be cleaned and contaminate it, or they can be discharged into the waste water unused. Embedding agents known from German patent specification DT 18 03 099, which consist of a mixture of solid acids or acidic salts and carbonates or bicarbonates and which disintegrate when water is added, improve the solvency, but are themselves very sensitive to moisture and therefore require additional protective measures.
Aus der europäischen Patentschrift EP 168 526 sind Enzymgranulate bekannt, die in Wasser quellfähige Stärke, Zeolith und wasserlösliches Granulierhilfsmittel enthalten. In diesem Dokument wird ein Herstellungsverfahren für derartige Formulierungen vorge¬ schlagen, das im wesentlichen darin besteht, eine von unlöslichen Bestandteilen befreite Fermenterlösung aufzukonzentrieren, mit den genannten Zuschlagstoffen zu versetzten, das entstandene Gemisch zu granulieren und gegebenenfalls das Granulat mit filmbildenden Polymeren und Farbstoffen zu umhüllen. Das Verfahren mit dem dort vorgeschlagenen Zu¬ schlagstoffgemisch wird vorteilhaft mit Fermentationslösungen durchgeführt, die auf einen relativ hohen Trockensubstanzgehalt, beispielsweise 55 Gew.-%, aufkonzentriert worden sind. Außerdem weisen die derart hergestellten Granulate eine so hohe Lösungs- be¬ ziehungsweise Zerfallsgeschwindigkeit unter Einsatzbedingungen auf, daß die Granulate teilweise schon bei der Lagerung relativ rasch zerfallen und die Enzyme desaktiviert wer¬ den.From the European patent EP 168 526 enzyme granules are known which contain starch which swells in water, zeolite and water-soluble granulation aid. In This document proposes a production process for such formulations, which essentially consists in concentrating a fermenter solution freed from insoluble constituents, adding the additives mentioned, granulating the resulting mixture and, if appropriate, coating the granules with film-forming polymers and dyes. The process with the additive mixture proposed there is advantageously carried out with fermentation solutions which have been concentrated to a relatively high dry matter content, for example 55% by weight. In addition, the granules produced in this way have such a high rate of dissolution or disintegration under operating conditions that the granules disintegrate relatively quickly even during storage and the enzymes are deactivated.
Aus der internationalen Patentanmeldung WO 92/11347 sind Enzymgranulate zum Einsatz in kömigen Wasch- und Reinigungsmitteln bekannt, die 2 Gew.-% bis 20 Gew.-% Enzym, 10 Gew.-% bis 50 Gew.-% quellfähige Stärke, 5 Gew.-% bis 50 Gew.-% wasserlösliches organisches Polymer als Granuherhilfsxnittel, 10 Gew.-% bis 35 Gew.-% Getreidemehl und 3 Gew.-% bis 12 Gew.-% Wasser enthalten. Durch ein derartiges Zuschlagstoffgemisch wird die Enzymverarbeitung ohne größere Aktivitätsverluste möglich und auch die Lager¬ beständigkeit der Enzyme in den Granulaten ist zufriedenstellend.From international patent application WO 92/11347, enzyme granules for use in granular detergents and cleaning agents are known which contain 2% by weight to 20% by weight of enzyme, 10% by weight to 50% by weight of swellable starch, 5% by weight .-% to 50 wt .-% water-soluble organic polymer as Granuherhilfsxnittel, 10 wt .-% to 35 wt .-% cereal and 3 wt .-% to 12 wt .-% water. Such an additive mixture enables enzyme processing without major loss of activity, and the storage stability of the enzymes in the granules is also satisfactory.
Ein insbesondere bei Reinigungsmitteln für das maschinelle Geschirrspülen weiteres Problem ist die Notwendigkeit, in derartige Mittel Korrosionsinhibitoren für Tafelsilber einzuarbeiten, insbesondere wenn die Mittel die in neuerer Zeit üblichen Bleich- be¬ ziehungsweise Oxidationsmittel auf Sauerstoffbasis enthalten. Silber kann beim Reinigen mit schwefelhaltigen Substanzen, die im Spülwasser gelöst beziehungsweise dispergiert sind, reagieren, denn bei der Reinigung von Geschirr in Haushaltsgeschirrspülmaschinen werden Speisereste und damit unter anderem auch Senf, Erbsen, Ei und sonstige schwefel¬ haltige Verbindungen wie Mercaptoaminosäuren in die Spülflotte eingebracht. Auch die während des maschinellen Spülens viel höheren Temperaturen und die längeren Kontakt¬ zeiten mit den schwefelhaltigen Speiseresten begünstigen im Vergleich zum manuellen Spülen das Anlaufen von Silber. Durch den intensiven Reinigungsprozeß in der Spülma- schine wird die Silberoberfläche außerdem vollständig entfettet und dadurch empfindlicher gegenüber chemischen Einflüssen.A further problem, particularly in the case of cleaning agents for machine dishwashing, is the need to incorporate corrosion inhibitors for silverware into such agents, particularly if the agents contain the bleaching or oxidizing agents based on oxygen which have been customary in recent times. Silver can react when cleaning with sulfur-containing substances that are dissolved or dispersed in the rinsing water, because when cleaning dishes in household dishwashers, food residues and thus, among other things, mustard, peas, egg and other sulfur-containing compounds such as mercaptoamino acids are introduced into the washing liquor . The much higher temperatures during machine rinsing and the longer contact times with the sulfur-containing food residues also favor the tarnishing of silver compared to manual rinsing. Due to the intensive cleaning process in the dishwashing The silver surface is also completely degreased, making it more sensitive to chemical influences.
Das Problem des Silberanlaufens wird insbesondere dann akut, wenn alternativ zu den schwefelhaltige Substanzen oxidativ "entschärfenden" Aktivchlorverbindungen Aktivsauer¬ stoffverbindungen, wie beispielsweise Natriumperborat oder Natriumpercarbonat einge¬ setzt werden, welche zur Beseitigung bleichbarer Anschmutzungen, wie beispielsweise Teeflecken/Teebeläge, Kaffeerückstände, Farbstoffe aus Gemüse, Lippenstiftreste und dergleichen dienen.The problem of tarnishing silver becomes particularly acute when, as an alternative to the sulfur-containing substances, oxidatively "defusing" active chlorine compounds, active oxygen compounds, such as sodium perborate or sodium percarbonate, are used which remove bleachable stains, such as tea stains / tea deposits, coffee residues, dyes Vegetables, remains of lipstick and the like serve.
Derartige Aktivsauerstoff-Bleichmittel werden, in der Regel zusammen mit Bleichaktivato¬ ren, vor allem in modernen niederalkalischen maschinellen Spülmitteln der neuen Reiniger¬ generation eingesetzt. Diese Mittel bestehen im allgemeinen aus den folgenden Funktionsbausteinen: Builderkomponente (Komplexbildner Dispergiermittel), Alkaliträger, Bleichsystem (Kombination aus Bleichmittel und Bleichaktivator), Enzym und Tensid. Unter den bei Einsatz derartig aufgebauter Mittel auftretenden Spülbedingungen bilden sich in Gegenwart von Silber in der Regel nicht nur sulfidische, sondern durch den oxi- dierenden Angriff* der intermediär gebildeten Peroxide beziehungsweise des Aktivsauer¬ stoffs auch oxidische Beläge auf den Silberoberflächen.Such active oxygen bleaching agents are used, generally together with bleach activators, especially in modern, low-alkaline machine dishwashing detergents of the new generation of cleaners. These agents generally consist of the following functional components: builder component (complexing agent dispersant), alkali carrier, bleaching system (combination of bleaching agent and bleach activator), enzyme and surfactant. Under the purging conditions that occur when such compositions are used, not only sulfidic deposits are formed in the presence of silver, but also oxidic deposits on the silver surfaces as a result of the oxidizing attack * of the intermediately formed peroxides or of the active oxygen.
Die Vermeidung der Silberkorrosion, das heißt die Bildung sulfidischer, oxidischer oder chloridischer Beläge auf Silber ist das Thema zahlreicher Veröffentlichungen. Aus der britischen Patentschrift GB 1 131 738 sind alkalische Geschirrspülmittel bekannt, die als Korrosionsinhibitor für Silber Benzotriazole enthalten. In der US-amerikanischen Patent¬ schrift US 3 549 539 werden stark alkalische, maschinell anwendbare Geschirreinigungs¬ mittel beschrieben, die als Oxidationsmittel unter anderem Perborat mit einem organischen Bleichaktivator enthalten können. Als Anlaufverhinderungsmittel werden Zusätze ebenfalls von Benzotriazol und auch Eisen(III)-chlorid empfohlen. In den europäischen Patent¬ schriften EP 135 226 und EP 135 227 werden schwach alkalische maschinell anwendbare Geschirrspülmittel mit einem Gehalt an Peroxyverbindungen und Aktivatoren beschrieben, die als Silberschutzmittel Benzotriazole und Fettsäuren enthalten können. Schließlich ist aus der deutschen Offenlegungsschrift DE 41 28 672 bekannt, daß Peroxyverbindungen, die durch Zusatz bekannter organischer Bleichaktivatoren aktiviert werden, in stark alka¬ lischen Reinigungsmitteln das Anlaufen von Silberteilen verhindern. Die deutschen Patent¬ anmeldungen DE 43 25 922 beziehungsweise DE 43 15 397 beschreiben die Verwendung von Titan-, Zirkonium-, Hafnium-, Vanadium-, Cobalt- oder Cersalzen und/oder -kom¬ plexen, in denen die Metalle in einer der Oxidationsstufen π, HL IV, V oder VI vorliegen, beziehungsweise von Mangan(II)salzen oder -komplexen zur Verhinderung der Silberkor¬ rosion. Die internationale Patentanmeldung WO 94/19445 beschreibt den Einsatz bestimm¬ ter Mangan(iπ)- oder Mangan(TV)-Komplexe als Silberkorrosionsschutzmittel in maschi¬ nellen Geschiπ-spül itteln. Die internationale Patentanmeldung WO 94/07981 offenbart die Verwendung von Cystein als Silberschutzmittel. In der deutschen Patentanmeldung 195 18 693.1 wird die süberkorrosionsinhibierende Wirkung von Cystin, allein oder insbe¬ sondere in Kombination mit Isocyanursäure, beschrieben.The avoidance of silver corrosion, that is, the formation of sulfidic, oxidic or chloride deposits on silver is the subject of numerous publications. From the British patent GB 1 131 738, alkaline dishwashing detergents are known which contain benzotriazoles as a corrosion inhibitor for silver. US Pat. No. 3,549,539 describes strongly alkaline, machine-applicable dishwashing detergents which can contain, inter alia, perborate with an organic bleach activator as the oxidizing agent. Additions of benzotriazole and iron (III) chloride are also recommended as anti-tarnish agents. European patent specifications EP 135 226 and EP 135 227 describe weakly alkaline machine dishwashing detergents containing peroxy compounds and activators, which may contain benzotriazoles and fatty acids as silver preservatives. Finally, it is known from German published patent application DE 41 28 672 that peroxy compounds, which are activated by the addition of known organic bleach activators, prevent the tarnishing of silver parts in strongly alkaline cleaning agents. German patent applications DE 43 25 922 and DE 43 15 397 describe the use of titanium, zirconium, hafnium, vanadium, cobalt or cerium salts and / or complexes in which the metals in one of the oxidation stages π, HL IV, V or VI are present, or of manganese (II) salts or complexes to prevent silver corrosion. The international patent application WO 94/19445 describes the use of certain manganese (iπ) or manganese (TV) complexes as silver corrosion inhibitors in mechanical dishwashing detergents. International patent application WO 94/07981 discloses the use of cysteine as a silver protection agent. German patent application 195 18 693.1 describes the supercorrosion-inhibiting action of cystine, alone or in particular in combination with isocyanuric acid.
Auch wenn die genannten Reinigungsmittel für Geschirr relativ wenig komplex zusammen¬ gesetzt sind, ist man dennoch bestrebt, im Rahmen ihrer Herstellung Komponenten einzusetzen, die mehr als einen der oben aufgeführten Wirkstoffe (Builder, Alkaliträger, Bleichsystem, Enzym, Tensid, Silberkorrosionsinhibitor) enthalten.Even if the cleaning agents mentioned for dishes are of relatively little complexity, efforts are nevertheless made to use components in their manufacture which contain more than one of the active ingredients listed above (builder, alkali carrier, bleaching system, enzyme, surfactant, silver corrosion inhibitor).
Die nicht vorveröffentlichte deutsche Patantanmeldung DE 43 44 215 betrifft für die Ein¬ arbeitung in insbesondere teilchenförmige Reinigungsmittel geeignete Enzymgranulate, enthaltend im Kern Enzym und anorganisches und/oder organisches Trägermaterial sowie gegebenenfalls Granulierhilfsmittel, auf den eine gleichmäßige Umhüllungsschicht aufge¬ bracht ist, welche einen insbesondere anorganischen Silberkorrosionsinhibitor enthält. Die¬ se Enzymgranulate können insbesondere durch das Aufbringen einer wäßrigen Lösung oder Dispersion, welche den Silberkorrosionsinhibitor enthält, auf einen enzymhaltigen Kern hergestellt werden. Ein solches Herstellverfahren bereitet bei der Verarbeitung was¬ serunlöslicher beziehungsweise schwer wasserlöslicher Silberkorrosionsinhibitoren Schwierigkeiten. Überdies wird zusätzliche Energie für die Verdampfung des mit dem Sil¬ berkorrosionsinhibitor aufgebrachten Wassers benötigt.The unpublished German patent application DE 43 44 215 relates to enzyme granules suitable for incorporation into particulate cleaning agents in particular, containing enzyme and inorganic and / or organic carrier material in the core and optionally granulating aids onto which a uniform coating layer has been applied, which in particular applies a coating layer contains inorganic silver corrosion inhibitor. These enzyme granules can be produced in particular by applying an aqueous solution or dispersion which contains the silver corrosion inhibitor to an enzyme-containing core. Such a manufacturing process creates difficulties in the processing of water-insoluble or sparingly water-soluble silver corrosion inhibitors. In addition, additional energy is required for the evaporation of the water applied with the silver corrosion inhibitor.
Es bestand daher die Aufgabe, ein Verfahren zu entwickeln, welches in der Lage ist, auf möglichst einfachem Wege ein enzymhaltiges Granulat, das zusätzlich Silber- korrosionsschutzmittel, beispielsweise in Form bestimmter organischer Substanzen enthält, herzustellen, in dem die genannten Komponenten, insbesondere das Enzym, lagerstabil sind.It was therefore the task to develop a process which is able to produce, in the simplest possible way, an enzyme-containing granulate which additionally contains silver Corrosion protection agent, for example in the form of certain organic substances, in which the components mentioned, in particular the enzyme, are stable in storage.
Das Wort "Korrosion" ist in seiner weitesten in der Chemie gebräuchlichen Bedeutung auszulegen, insbesondere soll hier "Korrosion" für jede visuell gerade noch erkennbare Veränderung einer Metalloberfläche, hier Silber, stehen, sei es zum Beispiel eine punktuelle Verfärbung, sei es zum Beispiel ein großflächiges Anlaufen.The word "corrosion" is to be interpreted in its broadest meaning in chemistry, in particular "corrosion" here should stand for any visually just recognizable change in a metal surface, here silver, be it for example a selective discoloration or be it for example large start-up.
Diese Aufgabe wird erfindungsgemäß durch ein für die Einarbeitung in insbesondere teilchenfbrmige Reinigungsmittel geeignetes silberkorrosionsinhibitorhaltiges Enzymgra¬ nulat, welches Enzym, anorganisches und/oder organisches Trägermaterial für das Enzym und Silberkorrosionsinhibitor sowie gegebenenfalls Granulierhilfsmittel in inniger, sozu¬ sagen homogener Abmischung enthält.According to the invention, this object is achieved by enzyme granulate containing silver corrosion inhibitor which is suitable for incorporation into particulate cleaning agents and which contains enzyme, inorganic and / or organic carrier material for the enzyme and silver corrosion inhibitor and optionally granulation aids in an intimate, so to say homogeneous mixture.
Zu den organischen Silberkorrosionsinhibitoren gehören Verbindungen mit trivalentem N- Atom wie Pyrazol, Thionalid, Morpholin, Melamin, Cystein, 2-Mercaptobenzodiazol, Di- stearylamin, Isocyanursäure, Bezotriazol, Aminotriazol, Aminotetrazol, Indazol sowie Imidazol und seine Derivate, zum Beispiel Benzimidazol, organische Disulfide, zum Bei¬ spiel Cystin, und zwei- sowie dreiwertige Phenole und deren Derivate, zum Beispiel Hydrochinon, Brenzkatechin, Phloroglucin, Gallussäure, Hydroxyhydrochinon und Pyro- gallol.The organic silver corrosion inhibitors include compounds with a trivalent N atom, such as pyrazole, thionalide, morpholine, melamine, cysteine, 2-mercaptobenzodiazole, distearylamine, isocyanuric acid, bezotriazole, aminotriazole, aminotetrazole, indazole and imidazole and its derivatives, for example organic benzimidazole Disulfides, for example cystine, and di- and trihydric phenols and their derivatives, for example hydroquinone, pyrocatechol, phloroglucinol, gallic acid, hydroxyhydroquinone and pyrogallol.
Beispiele für anorganische Silberkorrosionsinhibitoren sind Mangan-, Titan-, Zirkonium-, Hafnium-, Vanadium-, Cobalt- oder Cersalze und/oder -komplexe, in denen die genannten Metalle in einer der Oxidationsstufen II, HI, IV, V oder VI vorliegen. Die zur Salzbildung geeigneten Gegenionen umfassen alle üblichen ein-, zwei-, oder dreifach negativ geladenen anorganischen Anionen, zum Beispiel Oxid, Sulfat, Nitrat, Fluorid, aber auch organische Anionen wie zum Beispiel Stearat. Metallkomplexe im Sinne der Erfindung sind Verbin¬ dungen, die aus einem Zentralatom und einem oder mehreren Liganden sowie gegebenen¬ falls zusätzlich einem oder mehreren der obengenannten Anionen bestehen. Das Zentral¬ atom ist dabei eines der obengenannten Metalle in einer der obengenannten Oxidationsstu- fen. Die Liganden sind neutrale Moleküle oder Anionen, die ein- oder mehrzähnig sein können; der Begriff "Ligand" im Sinne der Erfindung ist beispielsweise in "Römpp Chemie Lexikon, Georg Thieme Verlag Stuttgart/New York, 9. Auflage, 1990, Seite 2507" näher erläutert. Ergänzen sich in einem Metallkomplex die Ladung des Zentralatoms und die La¬ dung des/der Liganden nicht auf Null, so sorgt, je nachdem, ob ein kationischer oder ein anionischer Ladungsüberschuß vorliegt, entweder eines oder mehrere der obengenannten Anionen oder ein oder mehrere Kationen, zum Beispiel Natrium-, Kalium- oder Ammo¬ niumionen, für den Ladungsausgleich. Bevorzugte Metallsalze oder Metallkomplexe sind MnSO4, V2O5, V2O4, VO2, TiOSO4, K2TiF6, K2ZrF6, CoSO4, Co(NO3)2, Ce(NO3)3 sowie deren Gemische. Bei diesen Salzen beziehungsweise Komplexen handelt es sich um handelsübliche Substanzen, die zum Zwecke des Silberkorrosions-Schutzes in der Regel ohne vorherige Reinigung eingesetzt werden können. So ist zum Beispiel das aus der SO3- Herstellung (Kontaktverfahren) bekannte oxidische Gemisch aus vier- und funfwertigem Vanadium (V2O5, VO2, V2O4) geeignet, ebenso wie das durch Verdünnen einer Ti(SO )2- Lösung mit Wasser entstehende Titanylsulfat TiOSO4.Examples of inorganic silver corrosion inhibitors are manganese, titanium, zirconium, hafnium, vanadium, cobalt or cerium salts and / or complexes in which the metals mentioned are present in one of the oxidation states II, HI, IV, V or VI. The counterions suitable for salt formation include all customary single, double or triple negatively charged inorganic anions, for example oxide, sulfate, nitrate, fluoride, but also organic anions such as stearate. For the purposes of the invention, metal complexes are compounds which consist of a central atom and one or more ligands and, if appropriate, additionally one or more of the above-mentioned anions. The central atom is one of the metals mentioned above in one of the oxidation states mentioned above. fen. The ligands are neutral molecules or anions, which can be monodentate or multidentate; the term “ligand” in the sense of the invention is explained in more detail, for example, in “Römpp Chemie Lexikon, Georg Thieme Verlag Stuttgart / New York, 9th edition, 1990, page 2507”. If the charge of the central atom and the charge of the ligand (s) do not add up to zero in a metal complex, then depending on whether there is a cationic or an anionic excess charge, either one or more of the abovementioned anions or one or more cations, for example sodium, potassium or ammonium ions, for charge balancing. Preferred metal salts or metal complexes are MnSO 4 , V 2 O 5 , V 2 O 4 , VO 2 , TiOSO 4 , K 2 TiF 6 , K 2 ZrF 6 , CoSO 4 , Co (NO 3 ) 2 , Ce (NO 3 ) 3 as well as their mixtures. These salts or complexes are commercially available substances that can generally be used for the purpose of protecting against silver corrosion without prior cleaning. For example, the oxidic mixture of tetravalent and pentavalent vanadium (V 2 O 5 , VO 2 , V 2 O 4 ) known from SO 3 production (contact process) is suitable, as is that by diluting a Ti (SO) 2 - Solution with titanyl sulfate TiOSO 4 .
Vorzugsweise ist im fertigen Enzymgranulat 0,5 Gew.-% bis 40 Gew.-%, insbesondere 1 Gew.-% bis 30 Gew.-% und besonders bevorzugt 2,5 Gew.-% bis 25 Gew.-% enzyma- tisches Protein, 30 Gew.-% bis 95 Gew.-%, insbesondere 40 Gew.-% bis 80 Gew.-% Trä¬ germaterial für das Enzym, gegebenenfalls 3 Gew.-% bis 12 Gew.-% Wasser und 0,5 Gew.-% bis 50 Gew.-%, insbesondere 5 Gew.- bis 30 Gew.-% Silberkorrosionsinhi¬ bitor enthalten.In the finished enzyme granulate, 0.5% by weight to 40% by weight, in particular 1% by weight to 30% by weight and particularly preferably 2.5% by weight to 25% by weight, is preferably enzymatic Protein, 30% by weight to 95% by weight, in particular 40% by weight to 80% by weight of carrier material for the enzyme, optionally 3% by weight to 12% by weight of water and 0.5 % By weight to 50% by weight, in particular 5% by weight to 30% by weight, of silver corrosion inhibitor.
Als Enzyme kommen in erster Linie die aus Mikroorganismen, wie Bakterien oder Pilzen, gewonnenen Proteasen, Lipasen, Cutinasen, Amylasen, Pullulanasen, Hemicellulasen, Cellulasen, Oxidasen und/oder Peroxidasen in Frage, wobei von Bacillus-Arten erzeugte Proteasen sowie ihre Gemische mit Amylasen bevorzugt sind. Sie werden in bekannter Weise durch Fermentationsprozesse aus geeigneten Mikroorganismen gewonnen, die zum Beispiel in den deutschen Offenlegungsschriften DE 1940488, DE 2044 161, DE 22 01 803 und DE 21 21 397, den US-amerikanischen Patentschriften US 3 632 957 und US 4264 738 sowie der europäischen Patentanmeldung EP 006638 beschrieben sind. Besonders vorteilhaft kann das erfindungsgemäße Verfahren zur Formulierung von sehr aktiven Proteasen, die beispielsweise aus der internationalen Patentanmeldung WO 91/02792 oder der US-amerikanischen Patentschrift US 5 340 735 bekannt sind, an¬ gewendet werden, weil deren lagerstabile Einarbeitung in Wasch- und Reinigungsmittel oft Probleme bereitet. Falls es sich bei dem erfindungsgemäßen Enzymgranulat um eine pro- teasehaltige Formulierung handelt, beträgt die Proteaseaktivität vorzugsweise 50 000 Pro- teaseeinheiten (PE, bestimmt nach der in Tenside 7 (1970), 125 beschriebenen Methode) bis 350 000 PE, insbesondere 100 000 PE bis 300 000 PE, pro Gramm Enzymgranulat.Enzymes primarily include the proteases, lipases, cutinases, amylases, pullulanases, hemicellulases, cellulases, oxidases and / or peroxidases obtained from microorganisms, such as bacteria or fungi, proteases produced by Bacillus species and their mixtures with amylases are preferred. They are obtained in a known manner by fermentation processes from suitable microorganisms, which are described, for example, in German patent applications DE 1940488, DE 2044 161, DE 22 01 803 and DE 21 21 397, US Pat. Nos. 3,632,957 and 4264 738 and European patent application EP 006638. The method according to the invention for the formulation of very active proteases, which are known, for example, from international patent application WO 91/02792 or US Pat. No. 5,340,735, are used because their storage-stable incorporation into detergents and cleaning agents often causes problems. If the enzyme granulate according to the invention is a protease-containing formulation, the protease activity is preferably 50,000 protease units (PE, determined by the method described in Tenside 7 (1970), 125) to 350,000 PE, in particular 100,000 PE up to 300,000 PE, per gram of enzyme granulate.
Zu den besonders bevorzugten Enzymgranulaten gemäß der Erfindung gehören solche, bei denen das Enzym Protease und der Silberkorrosionsinhibitor MnSO ist, oder bei denen das Enzym Protease und der Silberkorrosionsinhibitor Cystin ist, oder bei denen das Enzym Amylase und der Silberkorrosionsinhibitor Cystin ist.The particularly preferred enzyme granules according to the invention include those in which the enzyme protease and the silver corrosion inhibitor is MnSO, or in which the enzyme protease and the silver corrosion inhibitor is cystine, or in which the enzyme is amylase and the silver corrosion inhibitor cystine.
Als Trägermaterialien für das Enzym sind im Prinzip alle organischen oder anorganischen pulverförmigen Substanzen brauchbar, welche die zu granulierenden Enzyme nicht oder nur tolerierbar wenig zerstören oder desaktivieren und unter Granulationsbedingungen stabil sind. Zu derartigen Substanzen gehören beispielsweise Stärke, Getreidemehl, Cellu- losepulver, Alkalialumosilikat, insbesondere Zeolith, Schichtsilikat, zum Beispiel Bentonit oder Smectit, und wasserlösliche anorganische oder organische Salze, zum Beispiel Alkali¬ chlorid, Alkalisulfat, Alkalicarbonat oder Alkaliacetat, wobei Natrium oder Kalium die bevorzugten Alkalimetalle sind. Bevorzugt wird ein Trägermaterialgemisch- aus in Wasser quellfähiger Stärke, Getreidemehl und gegebenenfalls Cellulosepulver sowie Alkalicar¬ bonat eingesetzt.In principle, all organic or inorganic powdery substances which do not destroy or deactivate the enzymes to be granulated, or tolerably little, and which are stable under granulation conditions, can be used as carrier materials for the enzyme. Such substances include, for example, starch, cereal flour, cellulose powder, alkali alumosilicate, in particular zeolite, layered silicate, for example bentonite or smectite, and water-soluble inorganic or organic salts, for example alkali metal chloride, alkali metal sulfate, alkali metal carbonate or alkali metal acetate, sodium or potassium being the preferred alkali metals. A carrier material mixture of starch which is swellable in water, cereal flour and optionally cellulose powder and alkali carbonate is preferably used.
Bei der in Wasser quellfähigen Stärke handelt es sich vorzugsweise um Maisstärke, Reisstärke, Kartoffelstärke oder Gemische aus diesen, wobei der Einsatz von Maisstärke besonders bevorzugt ist. Quellfähige Stärke ist in den erfindungsgemäßen Enzymgranu¬ laten vorzugsweise in Mengen von 20 Gew.-% bis 50 Gew.-%, insbesondere von 25 Gew.-% bis 45 Gew.-% enthalten. Dabei beträgt die Summe der Mengen der quellfähi¬ gen Stärke und des Mehls vorzugsweise nicht über 80 Gew.-%, insbesondere 32 Gew.-% bis 65 Gew.-%. Bei dem Getreidemehl handelt es sich insbesondere um ein aus Weizen, Roggen, Gerste oder Hafer herstellbares Produkt oder um ein Gemisch dieser Mehle, wobei Vollkornmehle bevorzugt sind. Unter einem Vollkornmehl wird dabei ein nicht voll ausgemahlenes Mehl verstanden, das aus ganzen, ungeschälten Körnern hergestellt worden ist oder zumindest überwiegend aus einem derartigen Produkt besteht, wobei der Rest aus voll ausgemahle¬ nem Mehl beziehungsweise Stärke besteht. Vorzugsweise werden handelsübliche Weizen¬ mehl-Qualitäten, wie Type 450 oder Type 550, eingesetzt. Auch die Verwendung von Mehlprodukten der zu vorgenannten quellfähigen Stärken führenden Getreidearten ist möglich, wenn darauf geachtet wird, daß die Mehle aus den ganzen Körnern hergestellt worden sind. Durch die Mehlkomponente des Zuschlagstoffgemisches wird bekannter¬ maßen eine wesentliche Geruchsreduzierung der Enzymzubereitung erreicht, welche die Geruchsverminderung durch die Einarbeitung gleicher Mengen entsprechender Stärkearten bei weitem übertrifft. Derartiges Getreidemehl ist in den erfindungsgemäßen Enzymgra¬ nulaten vorzugsweise in Mengen von 5 Gew.-% bis 35 Gew.-%, insbesondere von 10 Gew.-% bis 25 Gew.-% enthalten.The starch which is swellable in water is preferably corn starch, rice starch, potato starch or mixtures thereof, the use of corn starch being particularly preferred. Swellable starch is contained in the enzyme granules according to the invention preferably in amounts of from 20% by weight to 50% by weight, in particular from 25% by weight to 45% by weight. The sum of the amounts of the swellable starch and the flour is preferably not more than 80% by weight, in particular 32% by weight to 65% by weight. The cereal flour is in particular a product which can be produced from wheat, rye, barley or oats or a mixture of these flours, wholemeal flours being preferred. A wholemeal flour is understood to mean a flour which has not been fully ground and which has been produced from whole, unpeeled grains or at least predominantly consists of such a product, the rest consisting of fully ground flour or starch. Commercial wheat flour qualities such as type 450 or type 550 are preferably used. It is also possible to use flour products from the cereals leading to the aforementioned swellable starches, provided that care is taken to ensure that the flours have been produced from the whole grains. The flour component of the additive mixture is known to achieve a substantial odor reduction in the enzyme preparation, which far exceeds the reduction in odor by incorporating the same amounts of corresponding starch types. Such cereal flour is contained in the enzyme granules according to the invention preferably in amounts from 5% by weight to 35% by weight, in particular from 10% by weight to 25% by weight.
Die erfindungsgemäßen Enzymgranulate enthalten als weitere Komponente des Trägerma¬ terials vorzugsweise 1 Gew.-% bis 50 Gew.-%, vorzugsweise 5 Gew.-% bis 25 Gew.- , bezogen auf gesamtes Granulat, eines Granulierhilfsmittelsystems, das Alkali-Carboxy- methylcellulose mit Substitutionsgraden von 0,5 bis 1 und Polyethylenglykol und/oder Alkylpolyethoxylat enthält. In diesem Granulierhilfsmittelsystem sind vorzugsweise, jeweils bezogen auf fertiges Enzymgranulat, 0,5 Gew.-% bis 5 Gew.-% Alkali-Carboxymethyl- cellulose mit Substitutionsgraden von 0,5 bis 1 und bis zu 3 Gew.-% Polyethylenglykol und/oder Alkylpolyethoxylat enthalten, wobei besonders bevorzugt ist, wenn mindestens 0,5 Gew.-%, insbesondere 0,8 Gew.-% bis 2 Gew.-% Polyethylenglykol mit einer mittleren Molmasse unter 1000 und/oder Alkylpolyethoxylat mit mindestens 30 Ethoxygruppen vorhanden ist, falls mehr als 2 Gew.-% Alkali-Carboxymethylcellulose enthalten ist.The enzyme granules according to the invention preferably contain, as a further component of the carrier material, 1% by weight to 50% by weight, preferably 5% by weight to 25% by weight, based on the total granulate, of a granulation aid system, the alkali carboxymethyl cellulose contains with degrees of substitution from 0.5 to 1 and polyethylene glycol and / or alkyl polyethoxylate. This granulation aid system preferably contains, based in each case on finished enzyme granules, 0.5% by weight to 5% by weight of alkali carboxymethyl cellulose with degrees of substitution from 0.5 to 1 and up to 3% by weight of polyethylene glycol and / or Contain alkyl polyethoxylate, it being particularly preferred if at least 0.5% by weight, in particular 0.8% by weight to 2% by weight, of polyethylene glycol with an average molecular weight below 1000 and / or alkyl polyethoxylate with at least 30 ethoxy groups is present, if more than 2% by weight of alkali carboxymethyl cellulose is contained.
Gegebenenfalls können als zusätzliche Bestandteile des Granulierhilfsmittelsystems auch weitere Cellulose- oder Stärkeether, wie Carboxymethylstärke, Methylcellulose, Hydroxy- ethylcellulose, Hydroxypropylcellulose sowie entsprechende Cellulosemischether, Gelatine, Casein, Traganth, Maltodextrose, Saccharose, Invertzucker, Glukosesirup oder andere in Wasser lösliche beziehungsweise gut dispergierbare Oligomere oder Polymere natürlichen oder synthetischen Ursprungs verwendet werden. Brauchbare synthetische wasserlösliche Polymere sind Polyacrylate, Polymethacrylate, Copolymere der Acrylsäure mit Malein¬ säure oder vinylgruppenhaltige Verbindungen, ferner Polyvinylalkohol, teilverseiftes Poly- vinylacetat und Polyvinylpyrrolidon. Soweit es sich bei den vorgenannten Verbindungen um solche mit freien Carboxylgruppen handelt, liegen sie normalerweise in Form ihrer Alkalisalze, insbesondere ihrer Natriumsalze vor. Derartige zusätzliche Granulierhilfsmittel können in den erfindungsgemäßen Enzymgranulaten in Mengen bis zu 10 Gew.-%, insbe¬ sondere von 0,5 Gew.-% bis 8 Gew.-% enthalten sein. Höhermolekulare Polyethylengly- kole, das heißt solche mit einem mittleren Molekulargewicht über 1000, sind zwar als syn¬ thetische wasserlösliche Polymere mit staubbindender Wirkung brauchbar, doch bewirken gerade die höhermolekularen Polyethylenglykole eine unerwünschte Erhöhung der be¬ nötigten Granulatauflösezeit, so daß diese Substanzen in den erfindungsgemäßen Enzym¬ granulaten vorzugsweise völlig fehlen.If necessary, additional cellulose or starch ethers, such as carboxymethyl starch, methyl cellulose, hydroxyethyl cellulose, hydroxypropyl cellulose and corresponding cellulose mixed ethers, gelatin, casein, tragacanth, maltodextrose, sucrose, invert sugar, glucose syrup or others can also be used as additional constituents of the granulation aid system Water-soluble or readily dispersible oligomers or polymers of natural or synthetic origin can be used. Usable synthetic water-soluble polymers are polyacrylates, polymethacrylates, copolymers of acrylic acid with maleic acid or compounds containing vinyl groups, furthermore polyvinyl alcohol, partially saponified polyvinyl acetate and polyvinyl pyrrolidone. Insofar as the aforementioned compounds are those with free carboxyl groups, they are normally in the form of their alkali metal salts, in particular their sodium salts. Such additional granulation aids can be contained in the enzyme granules according to the invention in amounts of up to 10% by weight, in particular from 0.5% by weight to 8% by weight. Higher molecular weight polyethylene glycols, that is to say those with an average molecular weight of more than 1000, can be used as synthetic water-soluble polymers with a dust-binding effect, but it is precisely the higher molecular weight polyethylene glycols which cause an undesirable increase in the granule dissolution time required, so that these substances can be used in the invention Enzyme granules are preferably completely absent.
In einer bevorzugten Ausführungsform weist das Enzymgranulat eine gleichmäßige äußere Umhüllungsschicht auf. Für die Umhüllungsschicht geeignet ist insbesondere ein Über¬ zugssystem, das 10 Gew.-% bis 30 Gew.-% feinteiliges anorganisches Pigment, 45 Gew - % bis 80 Gew.-% eines Alkohols oder Alkoholgemisches mit einem Schmelzpunkt im Bereich von 35 °C bis 75 °C, bis zu 15 Gew.-% Emulgator für den Alkohol, bis zu 5 Gew.-% Dispergiermittel für das Pigment und bis zu 5 Gew.-% Wasser enthält.In a preferred embodiment, the enzyme granules have a uniform outer coating layer. A coating system which contains 10% by weight to 30% by weight of finely divided inorganic pigment, 45% by weight to 80% by weight of an alcohol or alcohol mixture with a melting point in the range of 35 ° C. is particularly suitable for the coating layer up to 75 ° C, up to 15 wt .-% emulsifier for the alcohol, up to 5 wt .-% dispersant for the pigment and up to 5 wt .-% water.
Die Alkoholkomponente des Überzugssystems ist vorzugsweise ein primärer linearer Alkohol mit 14 bis 22 C- Atomen oder ein Gemisch aus diesen. Zu den genannten Alkoholen gehören insbesondere Myristylakohol, Cetylalkohol, Stearylalkohol, Arachidyl- alkohol, Behenylalkohol und ein- bis dreifach ungesättigte Alkohole entsprechender Ket¬ tenlänge, wobei wesentlich ist, daß die genannte Alkoholkomponente des Überzugs¬ systems einen Schmelzpunkt im Bereich von 35 °C bis 75 °C, insbesondere von 50 °C bis 60 °C aufweist, worunter hier die Temperatur verstanden werden soll, bei der beim Erwär¬ men 100 % der Alkoholkomponente in flüssiger Form vorliegen. Bei Einsatz von Alkohol¬ gemischen sind auch solche brauchbar, welche geringe Anteile, normalerweise unter 15 Gew.-% bezogen auf Alkoholgemisch, an bei Raumtemperatur flüssigen Anteilen ent- halten, solange das gesamte Alkoholgemisch bei Raumtemperatur fest erscheint und einen Erstarrungspunkt im obengenannten Temperaturbereich aufweist. Der Erstarrungspunkt ist die Temperatur, bei der beim Abkühlen auf eine Temperatur oberhalb des Schmelzpunkts erwämten Materials eine Verfestigung eintritt. Er kann mit Hilfe eines rotierenden Thermometers nach dem Verfahren der DIN ISO 2207 bestimmt werden.The alcohol component of the coating system is preferably a primary linear alcohol with 14 to 22 carbon atoms or a mixture of these. The alcohols mentioned include in particular myristyl alcohol, cetyl alcohol, stearyl alcohol, arachidyl alcohol, behenyl alcohol and mono- to tri-unsaturated alcohols of appropriate chain length, it being essential that the alcohol component of the coating system mentioned has a melting point in the range from 35 ° C. to 75 ° C, in particular from 50 ° C to 60 ° C, which is to be understood here as the temperature at which 100% of the alcohol component is present in liquid form when heated. When alcohol mixtures are used, it is also possible to use those which contain small proportions, normally below 15% by weight, based on the alcohol mixture, of proportions which are liquid at room temperature. hold as long as the entire alcohol mixture appears solid at room temperature and has a solidification point in the temperature range mentioned above. The solidification point is the temperature at which solidification occurs when the material which has been heated to a temperature above the melting point cools down. It can be determined with the help of a rotating thermometer according to the procedure of DIN ISO 2207.
Geeignete Emulgatoren für die Alkoholkomponente sind Substanzen, welche in der Lage sind, die Alkoholkomponente in Wasser zu emulgieren, so daß eine bei Temperaturen bis zu 95 °C versprühbare Mischung entsteht, und/oder welche es erlauben, das Umhüllungs¬ system in eine möglichst homogene, bei Temperaturen bis zu 120 °C versprühbare Schmel¬ ze zu überführen. Als Anhaltspunkt kann in diesem Zusammenhang dienen, daß Flüssigkei¬ ten mit Viskositäten bis zu etwa 10 000 mPa.s bei den genannten Temperaturen in der Re¬ gel problemlos mittels dafür vorgesehener Vorrichtungen versprüht und auf Enzymgranu¬ late aufgebracht werden können. Zu den Emulgatoren für die Alkoholkomponente des Überzugssystems gehören beispielsweise die Ethoxylierungsprodukte der genannten Alko¬ hole, wobei deren Umsetzungsprodukte mit durchschnittlich 25 bis 80, insbesondere 30 bis 45 Molequivalenten Ethylenoxid bevorzugt sind. Falls das Umhüllungssystem als wäßrige Dispersion auf das Enzymgranulat aufgebracht wird, sind unter den genannten Verbin¬ dungen solche mit Ethoxylierungsgraden von 25 bis 50, das heißt Umsetzungsprodukte mit 25 bis 50 Molequivalenten Ethylenoxid, bevorzugt. Alternativ oder zusätzlich zu den Al- koholethoxylaten können auch ethoxylierte Fettsäuren, wobei der Ethoxylierungsgrad vor¬ zugsweise 3 bis 9 beträgt, ethoxylierte Fettsäureamide, wobei der Ethoxylierungsgrad vor¬ zugsweise 4 bis 11 beträgt, und/oder Ethoxylierungsprodukte von Hydroxyfettsäureestem mit 1 bis 6 C-Atomen im Alkoholteil des Esters, beispielsweise Ricinolsäureglycerid, wo¬ bei der Ethoxylierungsgrad vorzugsweise 5 bis 80 insbesondere 20 bis 40 beträgt, als Emulgatorkomponente im Überzugssystem eingesetzt werden. Die Fettsäurekomponente der genannten Substanzen besitzt vorzugsweise 12 bis 22 C- Atome. Gewünschtenfalls können die Ethoxygruppen in den genannten Emulgatoren zumindest teilweise durch Prop- oxygruppen ersetzt sein.Suitable emulsifiers for the alcohol component are substances which are able to emulsify the alcohol component in water so that a mixture which can be sprayed at temperatures of up to 95 ° C. is obtained and / or which allow the coating system to be as homogeneous as possible to transfer meltable sprayable at temperatures up to 120 ° C. In this context, it can serve as a point of reference that liquids with viscosities of up to about 10,000 mPa.s can generally be sprayed without any problems at the temperatures mentioned by means of devices provided for this purpose and applied to enzyme granules. The emulsifiers for the alcohol component of the coating system include, for example, the ethoxylation products of the alcohols mentioned, their reaction products with an average of 25 to 80, in particular 30 to 45, molar equivalents of ethylene oxide being preferred. If the coating system is applied to the enzyme granulate as an aqueous dispersion, preferred among the compounds mentioned are those with degrees of ethoxylation of 25 to 50, that is to say reaction products with 25 to 50 molar equivalents of ethylene oxide. Alternatively or in addition to the alcohol ethoxylates, ethoxylated fatty acids, the degree of ethoxylation preferably being 3 to 9, ethoxylated fatty acid amides, the degree of ethoxylation preferably being 4 to 11, and / or ethoxylation products of hydroxy fatty acid esters having 1 to 6 C- Atoms in the alcohol part of the ester, for example ricinoleic acid glyceride, where the degree of ethoxylation is preferably 5 to 80, in particular 20 to 40, can be used as the emulsifier component in the coating system. The fatty acid component of the substances mentioned preferably has 12 to 22 carbon atoms. If desired, the ethoxy groups in the emulsifiers mentioned can be at least partially replaced by propoxy groups.
Zu den anorganischen Pigmenten, mit denen eventuelle störende Färbungen des Enzymgranulats überdeckt werden können, gehören beispielsweise Calciumcarbonat, Titandioxid, welches in Rutil- oder Anatase-Kristallmodifikation vorliegen kann, Zinkoxid, Zinksulfid, Bleiweiß (basisches Bleicarbonat), Bariumsulfat, Aluminiumhydroxid, Anti¬ monoxid, Lithopone (Zύιi sulfid-Bariurnsulfat), Kaolin, Kreide und/oder Glimmer. Diese liegen in so feinteiliger Form vor, daß sie in einer Schmelze der organischen Bestandteile des Überzugssystems oder in Wasser dispergiert werden können. Üblicherweise liegt die mittlere Teilchengröße derartiger Pigmente im Bereich von 0,004 μm bis 50 μm. Ins¬ besondere wenn das Pigment beziehungsweise das gesamte Überzugssystem in Form einer wäßrigen Dispersion eingesetzt werden soll, ist es bevorzugt, daß diese Dispersion Dispergiermittel für das Pigment und/oder, wie untenstehend beschrieben, den gewünsch- tenfalls im Überzugssystem enthaltenen zusätzlichen Silberkorrosionsinhibitor enthält. Der¬ artige Dispergiermittel können anorganisch, beispielsweise Alumiiiiumoxid oder Silizium¬ oxid, welche auch als Pigmente dienen können, oder organisch, beispielsweise Diethylen- glykol oder Dipropylenglykol, sein. Der Einsatz mit Dispergiermitteln oberflächenmodifi¬ zierter Pigmente ist ebenfalls möglich. Vorzugsweise wird mit AI-, Si-, Zr- oder Polyol- Verbindungen oberflächenmodifiziertes Titandioxidpigment, insbesondere in Rutilform, wie es beispielsweise unter den Handelsnamen Kronos® 2132 (Firma Kronos-Titan) oder Hombitan® R 522 (Firma Sachtleben Chemie GmbH) vertrieben wird, eingesetzt. Brauch¬ bar sind auch die Tiona® RLL-, AG- bzw. VC-Typen der Firma Solvay sowie die Bayertitan® RD-, R-KB- und AZ-Typen der Firma Bayer AG.The inorganic pigments with which possible disruptive coloring of the enzyme granulate can be covered include, for example, calcium carbonate, Titanium dioxide, which can be in rutile or anatase crystal modification, zinc oxide, zinc sulfide, lead white (basic lead carbonate), barium sulfate, aluminum hydroxide, anti-monoxide, lithopone (zinc sulfide-barium sulfate), kaolin, chalk and / or mica. These are in such a finely divided form that they can be dispersed in a melt of the organic constituents of the coating system or in water. The average particle size of such pigments is usually in the range from 0.004 μm to 50 μm. In particular if the pigment or the entire coating system is to be used in the form of an aqueous dispersion, it is preferred that this dispersion contains dispersing agents for the pigment and / or, as described below, the additional silver corrosion inhibitor which is optionally present in the coating system. Such dispersants can be inorganic, for example aluminum oxide or silicon oxide, which can also serve as pigments, or organic, for example diethylene glycol or dipropylene glycol. Use with dispersants of surface-modified pigments is also possible. Titanium dioxide pigment which is surface-modified with Al, Si, Zr or polyol compounds is preferred, in particular in rutile form, as is sold, for example, under the trade names Kronos® 2132 (Kronos-Titan) or Hombitan® R 522 (Sachtleben Chemie GmbH) , used. The Tiona® RLL, AG and VC types from Solvay and the Bayertitan® RD, R-KB and AZ types from Bayer AG can also be used.
In der gleichmäßigen Umhüllungsschicht kann auch, wie in DE 43 44 215 beschrieben, weiterer Silberkorrosionsinhibitor enthalten sein. In diesem Fall weist das Überzugssystem vorzugsweise einen Gehalt von mindestens 25 Gew.-% eines Silberkorrosionsinhibitors, insbesondere eines mit dem im Enzymkern enthaltenen Silberkorrosionsinhibitor nicht identischen Silberkorrosionsinhibitors, bis zu 30 Gew.-%, insbesondere 5 Gew.-% bis 25 Gew.-% feinteiligem anorganischem Pigment, 5 Gew.-% bis 75 Gew.-% bei Raumtem¬ peratur festem Alkohol mit einem Schmelzpunkt im Bereich von 35 °C bis 75 °C, bis zu 10 Gew.-%, insbesondere 1 Gew.-% bis 5 Gew.-% Emulgator für den Alkohol, bis zu 5 Gew.-%, insbesondere 0,2 Gew.-% bis 3 Gew.-% Dispergiermittel für das anorganische Pigment beziehungsweise den Silberkorrosionsinhibitor und bis zu 7 Gew.-% Wasser auf. Bevorzugt wird das silberkorrosionsinhibitorhaltige Enzymgranulat aus Gründen der höheren Enzymstabilität zumindest anteilsweise in Anlehnung an die einen Extrusions- schritt umfassenden Verfahren der internationalen Patentanmeldung WO 92/11347 be¬ ziehungsweise der deutschen Patentanmeldung DE 43 10 506 unter Einsatz quellfähiger Stärke, wasserlöslichem organischem Polymer und Getreidemehl hergestellt.Further silver corrosion inhibitor can also be contained in the uniform coating layer, as described in DE 43 44 215. In this case, the coating system preferably has a content of at least 25% by weight of a silver corrosion inhibitor, in particular a silver corrosion inhibitor which is not identical to the silver corrosion inhibitor contained in the enzyme core, up to 30% by weight, in particular 5% by weight to 25% by weight. % finely divided inorganic pigment, 5% by weight to 75% by weight at room temperature solid alcohol with a melting point in the range from 35 ° C. to 75 ° C., up to 10% by weight, in particular 1% by weight up to 5% by weight emulsifier for the alcohol, up to 5% by weight, in particular 0.2% by weight to 3% by weight of dispersant for the inorganic pigment or the silver corrosion inhibitor and up to 7% by weight of water on. For reasons of higher enzyme stability, the enzyme granules containing silver corrosion inhibitor are preferably produced, at least in part, based on the processes of international patent application WO 92/11347 comprising an extrusion step or German patent application DE 43 10 506 using swellable starch, water-soluble organic polymer and cereal flour .
Ein weiterer Gegenstand der Erfindung betrifft somit ein Verfahren zur Herstellung eines für die Einarbeitung in partikelformige Reinigungsmittel geeigneten silberkorrosions- inhibitorhaltigen Enzymgranulats durch Vermischen einer wäßrigen, das Enzym enthalten¬ den Flüssigkeit, die gegebenenfalls eine von unlöslichen Bestandteilen befreite und aufkon¬ zentrierte Fermentationsbrühe sein kann, mit anorganischem und/oder organischem Trägermaterial und dem Silberkorrosionsinhibitor, anschließende Extrusion der so erhalte¬ nen Mischung durch eine Lochplatte mit anschließendem Schneidegerät, gegebenenfalls Sphäronisierung des Extrudats in einem Rondiergerät sowie Trocknung, und gegebenen¬ falls Aufbringen eines gewünschtenfalls Farbstoff und oder Pigment enthaltenden Über¬ zugs. Ein solches Verfahren weist gegenüber bekannten Verfahren den Vorteil auf, daß so die Verarbeitung auch nicht oder nur wenig wasserlöslicher Silberkorrosionsinhibitoren möglich wird.Another object of the invention thus relates to a method for producing an enzyme granulate containing silver corrosion inhibitor suitable for incorporation into particulate cleaning agents by mixing an aqueous liquid containing the enzyme, which liquid can optionally be a fermentation broth freed from insoluble constituents and concentrated. with inorganic and / or organic carrier material and the silver corrosion inhibitor, subsequent extrusion of the mixture obtained in this way through a perforated plate with subsequent cutting device, optionally spheronization of the extrudate in a rounding device and drying, and, if appropriate, application of a dye and / or pigment-containing coating, if desired train Such a method has the advantage over known methods that it also makes it possible to process silver corrosion inhibitors which are insoluble or only slightly water-soluble.
Zur Herstellung der erfindungsgemäßen Enzymgranulate geht man vorzugsweise von Fer¬ mentbrühen aus, die beispielsweise durch Mikrofiltration von unlöslichen- Begleitstoffen befreit werden. Die Mikrofiltration wird dabei vorzugsweise als Querstrom-Mikrofiltration unter Verwendung poröser Rohre mit Mikroporen größer 0, 1 μm, Fließgeschwindigkeiten der Konzentratlösung von mehr als 2 m/s und einem Druckunterschied zur Permeatseite von unter 5 bar durchgeführt, wie beispielsweise in der europäischen Patentanmeldung EP 200 032 beschrieben. Anschließend wird das Mikrofiltrationspermeat vorzugsweise durch Ultrafiltration, gegebenenfalls mit anschließender Vakuumeindampfüng, aufkonzen¬ triert. Die Aufkonzentration kann dabei, wie in der internationalen Patentanmeldung WO 92/11347 beschrieben, so geführt werden, daß man nur zu relativ niedrigen Gehalten an Trockensubstanz von vorzugsweise 5 Gew.-% bis 50 Gew.-%, insbesondere von 10 Gew.-% bis 40 Gew.-% gelangt. Das Konzentrat wird einem zweckmäßigerweise zuvor hergestellten trockenen, pulverförmigen bis körnigen Gemisch der oben beschriebenen Zu- schlagstoffe, einschließlich des Silberkorrosionsinhibitors zudosiert und eingemischt. Der Wassergehalt der Mischung sollte so gewählt werden, daß sie sich bei der Bearbeitung mit Rühr- und Schlagwerkzeugen in körnige, bei Raumtemperatur nicht klebende Partikel überführen und bei Anwendung höherer Drücke plastisch verformen und extrudieren läßt. Das rieselfahige Vorgemisch wird im Prinzip bekannter Weise anschließend in einem Kneter sowie einem angeschlossenen Extruder zu einer plastischen, möglichst homogenen Masse verarbeitet, wobei als Folge der mechanischen Bearbeitung sich die Masse auf Temperaturen zwischen 40 °C und 60 °C, insbesondere 45 °C bis 55 °C erwärmen kann. Das den Extruder verlassende Gut wird durch eine Lochscheibe mit nachfolgendem Abschlagmesser geführt und dadurch zu zylinderfbrmigen Partikeln definierter Größe zer¬ kleinert. Zweckmäßigerweise beträgt der Durchmesser der Bohrungen in der Lochscheibe 0,7 mm bis 1,6 mm, vorzugsweise 0,8 mm bis 1,4 mm. Die in dieser Form vorliegenden Partikel können anschließend getrocknet und mit einem genannten Überzugssystem um¬ hüllt werden. Es hat sich jedoch als vorteilhaft erwiesen, die den Extruder und Zerhacker verlassenden zylindrischen Partikel vor dem Umhüllen zu sphäronisieren, das heißt sie in geeigneten Vorrichtungen abzurunden und zu entgraten. Man verwendet hierzu eine Vor¬ richtung, die aus einem zylindrischen Behälter mit stationären, festen Seitenwänden und einer bodenseitig drehbar gelagerten Reibplatte bestehen. Vorrichtungen dieser Art sind unter der Warenbezeichnung Marumerizer® in der Technik verbreitet und beispielsweise in den deutschen Auslegeschriften DE 21 37 042 und DE 21 37 043 beschrieben. An¬ schließend können eventuell auftretende staubfbrmige Anteile mit einer Korngröße unter 0, 1 mm, insbesondere unter 0,4 mm sowie eventuelle Grobanteile mit einer Korngröße über 2 mm, insbesondere über 1,6 mm durch Sieben oder Windsichten entfernt und gege¬ benenfalls in den Herstellungsprozess zurückgeführt werden. Nach der Sphäronisierung können die Kügelchen kontinuierlich oder chargenweise, vorzugsweise unter Verwendung einer Wirbelschichttrockenanlage, bei Zulufttemperaturen von vorzugsweise 35 °C bis 50 °C und insbesondere bei einer Produkttemperatur von nicht über 42 °C bis zum ge¬ wünschten Restfeuchtegehalt von beispielsweise 4 Gew.-% bis 10 Gew.-%, insbesondere 5 Gew.-% bis 8 Gew.-%, bezogen auf gesamtes Granulat, getrocknet werden. Nach oder vorzugsweise während der Trocknung kann das gegebenenfalls zusätzlichen Silberkorrosionsinhibitor enthaltende Überzugssystem als äußere Umhüllung aufgebracht werden. In einer Ausgestaltung des erfindungsgemäßen Herstellungsverfahrens wird das Überzugssystem als wäßrige Lösung beziehungsweise Dispersion, die vorzugsweise 30 Gew.-% bis 65 Gew.-% Wasser und 35 Gew.-% bis 70 Gew.-% des Überzugssystems enthält, wobei im Überzugssystem insbesondere 1 Gew.-% bis 2,5 Gew.-%, bezogen auf gesamtes Überzugssystem, Dispergiermittel für das Pigment und/oder den Silberkorrosi¬ onsinhibitor enthalten ist, in die Wirbelschicht aus Enzymextrudat eingebracht. Das über die wäßrige Dispersion zugeführte Wasser wird bei der gleichzeitig vorgenommenen oder einer anschließend erneut erforderlichen Trocknung wieder entfernt. In einer weiteren Ausgestaltung des erfindungsgemäßen Herstellungsverfahrens wird das Überzugssystem, gegebenenfalls unter Kühlung, als erwärmte, bei einer Temperatur von 5 °C bis 45 °C über dem Schmelzpunkt der Alkoholkomponente vorliegende Flüssigkeit auf das enzymhaltige Extrudat aufgebracht. Außerdem ist eine Kombination dieser Vorgehensweisen, die darin besteht, einen Teil des Überzugssystems in Form einer wäßrigen Lösung oder Dispersion und einen zweiten Teil in Form einer Schmelze aufzubringen, möglich. Vorzugsweise bringt man, bezogen auf fertiges Granulat, 10 Gew.-% bis 50 Gew.-% des Überzugs¬ systems als äußere Umhüllungsschicht auf das enzymhaltige Extrudat auf.The enzyme granules according to the invention are preferably prepared from fermentation broths which are freed of insoluble accompanying substances, for example by microfiltration. The microfiltration is preferably carried out as a cross-flow microfiltration using porous tubes with micropores larger than 0.1 μm, flow rates of the concentrate solution of more than 2 m / s and a pressure difference to the permeate side of less than 5 bar, as for example in the European patent application EP 200 032. The microfiltration permeate is then concentrated, preferably by ultrafiltration, if appropriate with subsequent vacuum evaporation. The concentration can, as described in international patent application WO 92/11347, be carried out in such a way that only relatively low dry matter contents of preferably 5% by weight to 50% by weight, in particular 10% by weight up to 40% by weight. The concentrate is expediently prepared beforehand in a dry, powdery to granular mixture of the additives described above. Impact substances, including the silver corrosion inhibitor, metered in and mixed in. The water content of the mixture should be selected so that it can be converted into granular particles which do not stick at room temperature when processed with stirring and striking tools and plastically deformed and extruded when using higher pressures. The free-flowing premix is, in principle, subsequently processed in a kneader and a connected extruder to form a plastic mass which is as homogeneous as possible Can heat 55 ° C. The material leaving the extruder is passed through a perforated disk with a subsequent knock-off knife and is thereby reduced to cylindrical particles of a defined size. The diameter of the bores in the perforated disk is expediently 0.7 mm to 1.6 mm, preferably 0.8 mm to 1.4 mm. The particles in this form can then be dried and coated with a coating system. However, it has proven to be advantageous to spheronize the cylindrical particles leaving the extruder and chopper before coating, that is to round them off and deburr them in suitable devices. For this purpose, a device is used which consists of a cylindrical container with stationary, fixed side walls and a friction plate rotatably mounted on the bottom. Devices of this type are widely used in technology under the Marumerizer® product name and are described, for example, in the German specifications DE 21 37 042 and DE 21 37 043. Any dusty particles with a grain size of less than 0.1 mm, in particular less than 0.4 mm, and any coarse particles with a grain size of more than 2 mm, in particular more than 1.6 mm, can then be removed by sieving or air separation and, if necessary, in the Manufacturing process can be traced. After spheronization, the beads can be added continuously or in batches, preferably using a fluidized bed drying unit, at supply air temperatures of preferably 35 ° C. to 50 ° C. and in particular at a product temperature of not more than 42 ° C. up to the desired residual moisture content of, for example, 4% by weight. % to 10% by weight, in particular 5% by weight to 8% by weight, based on the total granulate, are dried. After or preferably during drying, the coating system, which optionally contains additional silver corrosion inhibitor, can be applied as an outer covering. In one embodiment of the production process according to the invention, the coating system is in the form of an aqueous solution or dispersion which preferably contains 30% by weight to 65% by weight of water and 35% by weight to 70% by weight of the coating system, in particular 1 % By weight to 2.5% by weight, based on the entire coating system, of dispersant for the pigment and / or the silver corrosion inhibitor, is introduced into the fluidized bed of enzyme extrudate. The water supplied via the aqueous dispersion is removed during the drying which is carried out simultaneously or is subsequently necessary again. In a further embodiment of the production method according to the invention, the coating system, optionally with cooling, is applied to the enzyme-containing extrudate as a heated liquid at a temperature of 5 ° C. to 45 ° C. above the melting point of the alcohol component. In addition, a combination of these procedures, consisting in applying part of the coating system in the form of an aqueous solution or dispersion and a second part in the form of a melt, is possible. Preferably, based on the finished granulate, 10% by weight to 50% by weight of the coating system is applied to the enzyme-containing extrudate as an outer coating layer.
Eine weitere Ausgestaltung dieses Verfahrens umfasst die Herstellung von Enzymgranu¬ laten, welche zwei oder mehr verschiedene Enzyme enthalten. Dabei geht man vor¬ zugsweise so vor, daß man einen wie beschrieben durch Extrusion hergestellten, süber- korrosionsschutzmittelhaltigen Enzymkern mit einem teilchenformig konfektioniertem zweiten Enzym und gegebenenfalls weiteren teilchenformig konfektionierten Enzymen unter Agglomerationsbedingungen vermischt, wobei gegebenenfalls ein Bindemittel zum Einsatz kommt, und das Überzugsmaterial anschließend oder gleichzeitig aufbringt, wobei die mittlere Teilchengröße des das erste Enzym enthaltenden Extrudatkerns vorzugsweise das 1,1- bis 3-fache, insbesondere das 1,3- bis 2-fache derjenigen des zweiten oder weite¬ ren teilchenformig konfektionierten Enzyms beträgt. Diese Variante stützt sich auf das in der deutschen Patentanmeldung DE 43 29463 offenbarte Herstellungsverfahren für Mehr¬ enzymgranulate. Vorzugsweise handelt es sich bei dem Enzym im Extrudatkern um Protease und bei dem in den separat hergestellten, kleineren Teilchen, welche an das Extrudat agglomerieren, enthaltenen Enzym beziehungsweise bei den Enzymen, falls mehrere verschiedene kleinere Teilchen eingesetzt werden, um Amylase, Pullulanase, Lipase, Cutinase, Hemicellulase, Cellulase, Peroxidase und/oder Oxidase. Für den Einsatz in Geschirrspülniitteln sind silberkorrosionsinhibitorhaltige Mehrenzymgranulate, welche im Extrudatkern Protease und in den separat hergestellten, kleineren Teilchen Amylase und/oder Lipase enthalten, besonders bevorzugt.A further embodiment of this method comprises the production of enzyme granules which contain two or more different enzymes. The procedure is preferably such that an enzyme core containing super-anticorrosive agents, prepared as described by extrusion, is mixed with a second enzyme which has been made up in particulate form and, if appropriate, further enzymes made up in particulate form, under agglomeration conditions, a binder optionally being used, and the coating material is then used or applies simultaneously, the average particle size of the extrudate core containing the first enzyme preferably being 1.1 to 3 times, in particular 1.3 to 2 times that of the second or further enzyme-shaped enzyme. This variant is based on the production method for multi-enzyme granules disclosed in German patent application DE 43 29463. The enzyme in the extrudate core is preferably Protease and in the enzyme contained in the separately produced, smaller particles which agglomerate to the extrudate or in the enzymes, if several different smaller particles are used, to amylase, pullulanase, lipase, cutinase, hemicellulase, cellulase, peroxidase and / or Oxidase. For use in dishwashing detergents, multi-enzyme granules containing silver corrosion inhibitor, which contain protease in the extrudate core and amylase and / or lipase in the separately produced, smaller particles, are particularly preferred.
Die nach dem erfindungsgemäßen Verfahren erhaltene Enzymzubereitung besteht aus weitgehend abgerundeten, gleichmäßig umhüllten und staubfreien Partikeln, die in der Regel ein Schüttgewicht von etwa 500 bis 900 Gramm pro Liter, insbesondere 650 bis 880 Gramm pro Liter aufweisen. Die erfindungsgemäßen Granulate zeichnen sich durch eine sehr hohe Lagerstabilität, insbesondere bei Temperaturen über Raumtemperatur und hoher Luftfeuchtigkeit, sowie ein gutes Lösungsverhalten in der Reinigungsmittelflotte aus.The enzyme preparation obtained by the process according to the invention consists of largely rounded, uniformly coated and dust-free particles which generally have a bulk density of approximately 500 to 900 grams per liter, in particular 650 to 880 grams per liter. The granules according to the invention are notable for very high storage stability, in particular at temperatures above room temperature and high atmospheric humidity, and good dissolution behavior in the detergent liquor.
Das erfindungsgemäße oder nach dem erfindungsgemäßen Verfahren hergestellte Enzymgranulat wird vorzugsweise zur Herstellung fester, insbesondere teilchenförmiger Reinigungsmittel verwendet, die durch einfaches Vermischen der Enzymgranulate mit in derartigen Mitteln üblichen weiteren Pulverkomponenten erhalten werden können. Für die Einarbeitung in teilchenförmige Mittel weist das Enzymgranulat vorzugsweise mittlere Korngrößen im Bereich von 0,8 mm bis 1,6 mm auf. Die erfindungsgemäßen Granulate enthalten vorzugsweise weniger als 2 Gew.-%, insbesondere höchstens 1,4 Gew.-% an Partikeln mit Korngrößen außerhalb des Bereichs von 0,4 mm bis 1,6 mm.The enzyme granulate according to the invention or produced by the method according to the invention is preferably used for the production of solid, in particular particulate cleaning agents which can be obtained by simply mixing the enzyme granules with other powder components customary in such agents. For incorporation into particulate agents, the enzyme granules preferably have average grain sizes in the range from 0.8 mm to 1.6 mm. The granules according to the invention preferably contain less than 2% by weight, in particular at most 1.4% by weight, of particles with particle sizes outside the range from 0.4 mm to 1.6 mm.
Da sich die Silberkorrosionsinhibitoren wie oben ausgführt insbesondere zur Verhinderung der Silberkorrosion eignen, wenn sie in niederalkalischen Reinigern zum maschinellen Reinigen von Geschirr enthalten sind, ist ein weiterer Erfindungsgegenstand ein niederalkalisches Mittel zum maschinellen Reinigen von Geschirr, deren 1- gewichtsprozentige Lösung einen pH-Wert von 8 bis 11,5, vorzugsweise 9 bis 10,5 aufweist, enthaltend Enzym, Silberkorrosionsinhibitor, 15 Gew.-% bis 60 Gew.-%, vorzugsweise 30 Gew.-% bis 50 Gew.-% wasserlösliche Builderkomponente, 5 Gew.-% bis 25 Gew.-%, vorzugsweise 10 Gew.-% bis 15 Gew.-% Bleichmittel auf Sauerstoffbasis, 1 Gew.-% bis 10 Gew.-%, vorzugsweise 2 Gew.-% bis 6 Gew.-% Bleichaktivator, jeweils bezogen auf das gesamte Mittel, welches dadurch gekennzeichnet ist, daß es 0,1 Gew.-% bis 10 Gew.-%, insbesondere 0,5 Gew.-% bis 5 Gew.-% Enzymgranulat enthält, welches Enzym, anorganisches und/oder organisches Trägermaterial für das Enzym und Sil¬ berkorrosionsschutzmittel sowie gegebenenfalls Granulierhilfsmittel in inniger Abmischung enthält. Auch dabei sind organische Disulfide, zweiwertige Phenole, dreiwertige Phenole, Mangan-, Titan-, Zirkonium-, Hafiiium-, Vanadium-, Cobalt- oder Cersalze und/oder - komplexe, in denen die genannten Metalle in einer der Oxidationsstufen π, IQ, IV, V oder VI vorliegen, bevorzugte Silberkorrosionsinhibitoren.Since the silver corrosion inhibitors, as stated above, are particularly suitable for preventing silver corrosion when they are contained in lower-alkaline cleaners for machine cleaning of dishes, a further subject of the invention is a lower-alkaline agent for machine cleaning of dishes whose 1% by weight solution has a pH of 8 to 11.5, preferably 9 to 10.5, containing enzyme, silver corrosion inhibitor, 15% by weight to 60% by weight, preferably 30% by weight to 50% by weight of water-soluble builder component, 5% by weight % up to 25% by weight, preferably 10% by weight to 15% by weight of oxygen-based bleach, 1% by weight to 10% by weight, preferably 2% by weight to 6% by weight of bleach activator, in each case based on the total agent, which is characterized in that it contains 0.1% by weight to 10% by weight, in particular 0.5% by weight to 5% by weight, of enzyme granules, which enzyme, inorganic and / or contains organic carrier material for the enzyme and silver corrosion protection agent and optionally granulation aids in intimate mixture. Also here are organic disulfides, dihydric phenols, trihydric phenols, manganese, titanium, zirconium, hafiiium, vanadium, cobalt or cerium salts and / or - complexes in which the metals mentioned are in one of the oxidation states π, IQ, IV, V or VI are present, preferred silver corrosion inhibitors.
Als wasserlösliche Builderkomponenten in derartigen niederalkalischen Reinigungsmitteln kommen prinzipiell alle in maschinellen Geschirreinigungsmitteln üblicherweise einge¬ setzten Builder in Frage, zum Beispiel polymere Alkaliphosphate, die in Form ihrer alka¬ lischen neutralen oder sauren Natrium- oder Kaliumsalze vorliegen können. Beispiele hier¬ für sind Tetranatriumdiphosphat, Dinatriumdihydrogendiphosphat, Pentanatriurntri- phosphat, sogenanntes Natriumhexametaphosphat sowie die entsprechenden Kaliumsalze beziehungsweise Gemische aus Natrium- und Kaliumsalzen. Ihre Mengen können im Bereich von bis zu etwa 35 Gew.-%, bezogen auf das gesamte Mittel liegen; vorzugsweise sind die erfindungsgemäßen Mittel jedoch frei von solchen Phosphaten. Weitere mögliche wasserlösliche Builderkomponenten sind zum Beispiel organische Polymere nativen oder synthetischen Ursprungs, vor allem Polycarboxylate, die insbesondere in Hartwasserregio- nen als Co-Builder wirken. In Betracht kommen beispielsweise Polyacrylsäuren und Copolymere aus Maleinsäureanhydrid und Acrylsäure sowie die Natriumsalze dieser Polymersäuren. Handelsübliche Produkte sind zum Beispiel Sokalan® CP 5 und PA 30 der Firma BASF. Zu den als Co-Builder brauchbaren Polymeren nativen Ursprungs gehören beispielsweise oxidierte Stärke, wie zum Beispiel aus der internationalen Patentanmeldung WO 94/05762 bekannt, und Polyaminosäuren wie Polyglutaminsäure oder Polyasparagin- säure. Weitere mögliche Builderkomponenten sind natürlich vorkommende Hydroxycar- bonsäuren wie zum Beispiel Mono-, Dihydroxybernsteinsäure, α-Hydroxypropionsäure und Gluconsäure. Zu den bevorzugten Builderkomponenten gehören die Salze der Citro- nensäure, insbesondere Natriumeitrat. Als Natriumeitrat kommen wasserfreies Trina- triumeitrat und vorzugsweise Trinatriumcitratdihydrat in Betracht. Trinatriumcitratdihydrat kann als fein- oder grobkristallines Pulver eingesetzt werden. In Abhängigkeit vom letzt¬ lich in den erfindungsgemäßen Mitteln eingestellten pH- Wert können auch die zu den ge¬ nannten Co-Builder-Salzen korrespondierenden Säuren vorliegen.In principle, all builders typically used in machine dishwashing detergents, for example polymeric alkali metal phosphates, which can be present in the form of their alkaline neutral or acidic sodium or potassium salts, are suitable as water-soluble builder components in such low-alkaline cleaning agents. Examples of this are tetrasodium diphosphate, disodium dihydrogen diphosphate, pentasodium tri-phosphate, so-called sodium hexametaphosphate and the corresponding potassium salts or mixtures of sodium and potassium salts. Their amounts can range up to about 35% by weight, based on the total agent; however, the agents according to the invention are preferably free of such phosphates. Other possible water-soluble builder components are, for example, organic polymers of native or synthetic origin, especially polycarboxylates, which act as co-builders, in particular in hard water regions. For example, polyacrylic acids and copolymers of maleic anhydride and acrylic acid and the sodium salts of these polymer acids are suitable. Commercial products are, for example, Sokalan® CP 5 and PA 30 from BASF. Polymers of native origin that can be used as co-builders include, for example, oxidized starch, as known, for example, from international patent application WO 94/05762, and polyamino acids such as polyglutamic acid or polyaspartic acid. Other possible builder components are naturally occurring hydroxycarboxylic acids such as, for example, mono-, dihydroxysuccinic acid, α-hydroxypropionic acid and gluconic acid. The preferred builder components include the salts of the citro- Nenoic acid, especially sodium citrate. Anhydrous trisodium citrate and preferably trisodium citrate dihydrate are suitable as sodium citrate. Trisodium citrate dihydrate can be used as a fine or coarse crystalline powder. Depending on the pH finally set in the agents according to the invention, the acids corresponding to the co-builder salts mentioned can also be present.
Als Bleichmittel auf Sauerstoffbasis kommen in erster Linie Natriumperboratmono- be¬ ziehungsweise -tetrahydrat und/oder Natriumpercarbonat in Betracht. Der Einsatz von Na- triumpercarbonat hat Vorteile, da sich dieses besonders günstig auf das Korrosionsver¬ halten an Gläsern auswirkt. Das Bleichmittel auf Sauerstoffbasis ist deshalb vorzugsweise ein Percarbonat-Salz, insbesondere Natriumpercarbonat. Da Bleichmittel auf Sauerstoffba- sis in der Regel erst bei erhöhten Temperaturen ihre volle Wirkung entfalten, werden zu ihrer Aktivierung bei ca. 60°C und darunter, das heißt der ungefähren Temperaturen des Reinigungsprozesses in der GeschÜTspülmaschine, sogenannte Bleichaktivatoren einge¬ setzt. Als Bleichaktivatoren können zum Beispiel Pentaacetylglucose, l,5-Diacetyl-2,2- dioxo-hexahydro-l,3,5-triazin (DADHT) und/oder Isatosäureanhydrid dienen, vorzugs¬ weise jedoch N,N,N', -Tetraacetylethylendiamin (TAED). Alternativ können auch bekannte Peroxycarbonsäuren, zum Beispiel Dodecandipersäure oder Phthalimidopercar- bonsäuren, die gegebenenfalls am Aromaten substituiert sein können, enthalten sein. Überdies kann auch der Zusatz geringer Mengen bekannter Bleichmittelstabilisatoren wie beispielsweise von Phosphonaten, Boraten beziehungsweise Metaboraten" und Metasili- katen sowie Magnesiumsalzen wie Magnesiumsulfat zweckdienlich sein.Suitable oxygen-based bleaches are primarily sodium perborate mono- or tetrahydrate and / or sodium percarbonate. The use of sodium percarbonate has advantages, since this has a particularly favorable effect on the corrosion behavior on glasses. The oxygen-based bleach is therefore preferably a percarbonate salt, especially sodium percarbonate. Since bleaching agents based on oxygen generally only develop their full effect at elevated temperatures, so-called bleach activators are used to activate them at about 60 ° C. and below, that is to say the approximate temperatures of the cleaning process in the dishwasher. Pentaacetylglucose, l, 5-diacetyl-2,2-dioxo-hexahydro-l, 3,5-triazine (DADHT) and / or isatoic anhydride, for example, can be used as bleach activators, but preferably N, N, N ', tetraacetylethylenediamine (TAED). Alternatively, known peroxycarboxylic acids, for example dodecanediperic acid or phthalimidopercarboxylic acids, which can optionally be substituted on the aromatic, can also be present. In addition, the addition of small amounts of known bleach stabilizers such as, for example, phosphonates, borates or metaborates " and metasilicates and magnesium salts such as magnesium sulfate can also be useful.
Vorzugsweise enthalten die erfindungsgemäßen Mittel die in üblichen niederalkalischen maschinellen Geschirreinigungsmitteln enthaltenen Alkaliträger wie zum Beispiel Alkali¬ silikate, Alkalicarbonate und/oder Alkalihydrogencarbonate. Zu den üblicherweise einge¬ setzten Alkaliträgern zählen Carbonate, Hydrogencarbonate und Alkalisilikate mit einem Molverhältnis SiO2/M2O (M = Alkaliatom) von 1,5 : 1 bis 2,5 : 1. Alkalisilikate können dabei in Mengen von bis zu 30 Gew.-%, bezogen auf das gesamte Mittel, enthalten sein. Auf den Einsatz der hoch alkalischen Metasilikate als Alkaliträger wird vorzugsweise ganz verzichtet. Das in den erfindungsgemäßen Mitteln bevorzugt eingesetzte Alkaliträger¬ system ist ein Gemisch aus Carbonat und Hydrogencarbonat, vorzugsweise Natrium- carbonat und -hydrogencarbonat, das in einer Menge von bis zu 60 Gew.-%, vorzugsweise 10 Gew.-% bis 40 Gew.- , enthalten ist. Je nachdem, welcher pH- Wert letztendlich ge¬ wünscht wird, variiert das Verhältnis von eingesetztem Carbonat und eingesetztem Hydro¬ gencarbonat, üblicherweise wird jedoch ein Überschuß an Natriumhydrogencarbonat eingesetzt, so daß das Gewichtsverhältnis zwischen Hydrogencarbonat und Carbonat im allgemeinen 1 : 1 bis 15 : 1 beträgt.The agents according to the invention preferably contain the alkali carriers, such as, for example, alkali silicates, alkali carbonates and / or alkali bicarbonates, contained in customary low-alkaline machine dishwashing detergents. The alkali carriers usually used include carbonates, hydrogen carbonates and alkali silicates with a SiO 2 / M 2 O (M = alkali atom) molar ratio of 1.5: 1 to 2.5: 1. Alkali silicates can be used in amounts of up to 30% by weight .-%, based on the total agent, may be included. The use of the highly alkaline metasilicates as alkali carriers is preferably avoided entirely. The alkali carrier system preferably used in the agents according to the invention is a mixture of carbonate and bicarbonate, preferably sodium carbonate and bicarbonate, which is contained in an amount of up to 60% by weight, preferably 10% by weight to 40% by weight. Depending on which pH value is ultimately desired, the ratio of carbonate and hydrogen carbonate used varies, but an excess of sodium hydrogen carbonate is usually used, so that the weight ratio between hydrogen carbonate and carbonate is generally 1: 1 to 15: 1 is.
Zusätzlich können die erfindungsgemäßen Mittel in fester Form konfektionierte Enzyme wie Proteasen, Amylasen, Lipasen und Cellulasen enthalten, die nicht in Form des erfindungsgemäßen Granulates vorliegen, beispielsweise Proteasen wie BLAP®, Opti- ase®, Opticlean®, Maxacal®, Maxapem®, Esperase® und/oder Savinase®, Amylasen wie Termamyl®, Amylase-LT® und/oder Maxamyl®, Lipasen wie Lipolase®, Lipomax®, Lumafast® und/oder Lipozym®, Cellulasen wie Celluzym® und/oder KAC®.In addition, the agents according to the invention can contain ready-made enzymes such as proteases, amylases, lipases and cellulases which are not in the form of the granules according to the invention, for example proteases such as BLAP®, Optiase®, Opticlean®, Maxacal®, Maxapem®, Esperase ® and / or Savinase®, amylases like Termamyl®, Amylase-LT® and / or Maxamyl®, lipases like Lipolase®, Lipomax®, Lumafast® and / or Lipozym®, cellulases like Celluzym® and / or KAC®.
Den erfindungsgemäßen Mitteln können gegebenenfalls auch Tenside, insbesondere schwach schäumende nichtionische Tenside zugesetzt werden, die der besseren Ablösung fetthaltiger Speisereste, als Netzmittel und gegebenfalls im Rahmen der Herstellung der Reinigungsmittel als Granulierhilfsmittel dienen. Ihre Menge kann bis zu 5 Gew.-%, vor¬ zugsweise bis zu 2 Gew.-% betragen. Üblicherweise werden insbesondere in Reinigungs¬ mitteln für den Einsatz in maschinellen Geschirrspülverfahren extrem schaumarme Verbin¬ dungen eingesetzt. Hierzu zählen vorzugsweise Cι2-Cιg-Alkylpolyethylenglykol-poly- propylenglykolether mit jeweils bei zu 8 Mol Ethylenoxid- und Propylenoxideinheiten im Molekül. Man kann aber auch andere bekannt schaumarme nichtionische Tenside verwenden, wie zum Beispiel Cπ-Cis-Alkylpolyethylenglykol-polybutylenglykolether mit jeweils bis zu 8 Mol Ethylenoxid- und Butylenoxideinheiten im Molekül, endgruppenver- schlossene Alkylpolyalkylenglykolmischether sowie die zwar schäumenden, aber ökolo¬ gisch attraktiven Cg-CH-Alkylpolyglucoside mit einem Polymerisierungsgrad von etwa 1 bis 4 (z. B. APG® 225 und APG® 600 der Firma Henkel) und/oder Cι2-C14-Alkyl- polyethylenglykole mit 3 bis 8 Ethylenoxideinheiten im Molekül. Ebenfalls geeignet sind Tenside aus der Familie der Glucamide wie zum Beispiel Alkyl-N-Methyl-Glucamide, in denen der Alkylteil bevorzugt aus einem Fettalkohol mit der C-Kettenlänge Cβ-Cu stammt. Es ist teilweise vorteilhaft, wenn die beschriebenen Tenside als Gemische eingesetzt wer- den, zum Beispiel die Kombination Alkylpolyglykosid mit Fettalkoholethoxylaten oder Glucamid mit Alkylpolyglykosiden.If appropriate, surfactants, in particular low-foaming nonionic surfactants, can also be added to the agents according to the invention, which serve to better detach fatty food residues, as wetting agents and, if appropriate, as granulating aids in the course of the preparation of the cleaning agents. Their amount can be up to 5% by weight, preferably up to 2% by weight. Extremely low-foaming compounds are usually used in particular in cleaning agents for use in machine dishwashing processes. These preferably include C 2 -C alkyl polyglycol-propylene glycol ether, each with up to 8 moles of ethylene oxide and propylene oxide units in the molecule. But you can also use other known low-foaming nonionic surfactants, such as Cπ-Cis-alkylpolyethylene glycol-polybutylene glycol ether, each with up to 8 moles of ethylene oxide and butylene oxide units in the molecule, end-capped alkylpolyalkylene glycol mixed ethers and the foaming but ecologically attractive Cg- C H alkyl polyglucosides with a degree of polymerization of about 1 to 4 (eg APG® 225 and APG® 600 from Henkel) and / or C 2 -C 14 alkyl polyethyleneglycols with 3 to 8 ethylene oxide units in the molecule. Also suitable are surfactants from the family of glucamides, such as, for example, alkyl-N-methyl-glucamides, in which the alkyl part preferably comes from a fatty alcohol with the C chain length Cβ-Cu. It is sometimes advantageous if the surfactants described are used as mixtures den, for example the combination of alkyl polyglycoside with fatty alcohol ethoxylates or glucamide with alkyl polyglycosides.
Sofern die Reinigungsmittel bei der Anwendung zu stark schäumen, können ihnen noch bis zu 6 Gew.-%, vorzugsweise etwa 0,5 Gew.-% bis 4 Gew.-% einer schaumdrückenden Verbindung, vorzugsweise aus der Gruppe der Silikonöle, Gemische aus Silikonöl und hydrophobierter Kieselsäure, Paraffine, Parafin-Alkohol-Kombinationen, hydrophobierter Kieselsäure, der Bisfettsäureamide, und sonstiger weiterer bekannter im Handel erhältliche Entschäumer zugesetzt werden. Weitere fakultative Inhaltsstoffe in den erfindungsge¬ mäßen Mitteln sind zum Beispiel Parfümöle.If the cleaning agents foam too much during use, they can still contain up to 6% by weight, preferably about 0.5% by weight to 4% by weight, of a foam-suppressing compound, preferably from the group of silicone oils, mixtures of silicone oil and hydrophobicized silica, paraffins, paraffin-alcohol combinations, hydrophobicized silica, the bisfatty acid amides, and other other known commercially available defoamers. Other optional ingredients in the agents according to the invention are, for example, perfume oils.
Die erfindungsgemäßen Geschirrspülmittel liegen vorzugsweise als pulverförmige, granuläre oder tablettenförmige Präparate vor, die in an sich bekannter Weise, beispiels¬ weise durch Mischen, Granulieren, Walzenkompaktieren und/oder durch Sprühtrocknung der thermisch belastbaren Komponenten und Zumischen der empfindlicheren Komponen¬ ten, zu denen insbesondere das erfindungsgemäße Enzymgranulat zu rechnen ist, herge¬ stellt werden können.The dishwashing detergents according to the invention are preferably in the form of powdery, granular or tablet-like preparations which, in a manner known per se, for example by mixing, granulating, roller compacting and / or by spray drying the thermally loadable components and admixing the more sensitive components, to which in particular the enzyme granulate according to the invention is to be expected, can be produced.
Zur Herstellung von erfindungsgemäßen Reinigungsmitteln in Tablettenform geht man vor¬ zugsweise derart vor, daß man alle Bestandteile in einem Mischer miteinander vermischt und das Gemisch mittels herkömmlicher Tablettenpressen, beispielsweise Exzenterpressen oder Rundläuferpressen, mit Preßdrucken im Bereich von 200 105 Pa bis 1 500 105 Pa verpresst. Man erhält so problemlos bruchfeste und dennoch unter Anwendungsbe¬ dingungen ausreichend schnell lösliche Tabletten mit Biegefestigkeit von normalerweise über 150 N. Vorzugsweise weist eine derart hergestellte Tablette ein Gewicht von 15 g bis 40 g, insbesondere von 20 g bis 30 g auf, bei einem Durchmesser von 35 mm bis 40 mm.For the preparation of cleaning agents according to the invention in tablet form, the procedure is preferably such that all constituents are mixed with one another in a mixer and the mixture by means of conventional tablet presses, for example eccentric presses or rotary presses, with pressing pressures in the range from 200 10 5 Pa to 1 500 10 5 Pa pressed. In this way, break-resistant tablets are obtained which, under application conditions, dissolve sufficiently quickly and have a flexural strength of normally over 150 N. A tablet produced in this way preferably has a weight of 15 g to 40 g, in particular 20 g to 30 g, with a diameter from 35 mm to 40 mm.
Die Herstellung erfindungsgemäßer Geschirrspülmittel in Form von nicht staubenden, lagerstabil rieselfahigen Pulvern und/oder Granulaten mit hohen Schüttdichten im Bereich von 800 bis 1000 g/1 kann dadurch erfolgen, daß man in einer ersten Verfahrensteilstufe die Builder-Komponenten mit wenigstens einem Anteil flüssiger Mischungskomponenten unter Erhöhung der Schüttdichte dieses Vorgemisches vermischt und nachfolgend - ge- wünschtenfalls nach einer Zwischentrocknung - die weiteren Bestandteile des Mittels, darunter die silberkorrosionsinhibitorhaltigen Enzymgranulate, mit dem so gewonnenen Vorgemisch vereinigt.Dishwashing detergents according to the invention in the form of non-dusting, storage-stable, free-flowing powders and / or granules with high bulk densities in the range from 800 to 1000 g / 1 can be carried out by adding the builder components with at least a proportion of liquid mixture components in a first process stage Increase in the bulk density of this premixed mixture and subsequently - if desired after an intermediate drying - the other constituents of the agent, including the enzyme granules containing silver corrosion inhibitor, combined with the premix obtained in this way.
Die Mittel können sowohl in Haushaltsgeschiirspülmaschinen wie in gewerblichen Spülmaschinen eingesetzt werden. Die Zugabe erfolgt von Hand oder mittels geeigneter Dosiervorrichtungen. Die Anwendungskonzentrationen in der Reinigungsflotte betragen in der Regel etwa 1 bis 8 g/1, vorzugsweise 2 bis 5 g/1.The agents can be used both in household dishwashers and in commercial dishwashers. It is added by hand or using suitable dosing devices. The application concentrations in the cleaning liquor are generally about 1 to 8 g / 1, preferably 2 to 5 g / 1.
Ein maschinelles Spülprogramm wird im allgemeinen durch einige auf den Reinigungsgang folgende Zwischenspülgänge mit klarem Wasser und einem Klarspülgang mit einem gebräuchlichem Klarspülmittel ergänzt und beendet. Nach dem Trocknen erhält man beim Einsatz erfindungsgemäßer Mittel nicht nur ein völlig sauberes und in hygienischer Hinsicht einwandfreies Geschirr, sondern vor allem auch hellglänzende Silberbesteckteile. A machine wash program is generally supplemented and ended by a few intermediate rinse cycles with clear water and a rinse cycle with a customary rinse aid after the cleaning cycle. After drying, when using the agents according to the invention, not only are completely clean dishes which are impeccable from a hygienic point of view, but above all also bright silver cutlery items.
Beispielexample
Ein nach Fermentation, Entfernung der Fermentationsrückstände durch Dekantieren, Mikrofiltration in einer Ultrafiltrationsanlage und weiterer Aufkonzentrierung mittels Vakuumeindampfüng wie in der internationalen Patentanmeldung WO 91/02792 beschrie¬ ben erhaltenes wäßriges Proteasekonzentrat wurde mit den in der nachfolgenden Tabelle angegebenen Zuschlagstoffen in einem Labormischer der Firma Lödige® homogen ver¬ mischt und mit Hilfe eines Extruders mit Schneidevorrichtung in Granulate überführt.An aqueous protease concentrate obtained after fermentation, removal of the fermentation residues by decanting, microfiltration in an ultrafiltration system and further concentration by means of vacuum evaporation as described in international patent application WO 91/02792 was mixed with the additives listed in the table below in a laboratory mixer from Lödige® homogeneously mixed and converted into granules with the aid of an extruder with a cutting device.
Tabelle 1 : Einsatzmengen [Gew.-%]Table 1: Amounts used [% by weight]
Proteasekonzentrat 22Protease concentrate 22
Polyethylenglykol* 3Polyethylene glycol * 3
Zellulosepulverb) 6,5Cellulose powder b) 6.5
Saccharose 3,5Sucrose 3.5
Carboxymethylcellulose 7Carboxymethyl cellulose 7
Weizenmehl T 450 15Wheat flour T 450 15
Maisstärke 33Corn starch 33
L-Cystinc) 10L-cystine c) 10
a) mittleres Molgewicht 400 b) Technocel® 30 c) Lieferant Freedom Chemical Diamalt GmbHa) average molecular weight 400 b) Technocel® 30 c) supplier Freedom Chemical Diamalt GmbH
Der Lochdurchmesser der Lochplatte des Extruders betrug 0,8 mm. Das Verhältnis von Länge zu Dicke des Granulatkorns lag bei 1. Nach der Verrundung und Trocknung der Granulate in einem Wirbelschichttrockner wurden die Partikel mit Teilchengrößen kleiner 0,4 mm und größer 1,6 mm abgesiebt. Die Kornfraktion zwischen 0,4 mm und 1,6 mm wurde in einem Kugelcoater mit Turbojet- System der Firma Hüttlin mit einer Umhüllungs- schicht überzogen, wobei eine Schmelze aus 70 Gew.-% technischem Stearylalkohol, 6 Gew.-% 40 fach ethoxyliertem Talgfettalkohol und 24 Gew.-% Titandioxid zum Einsatz kam. Das erhaltene silberschutzmittelhaltige Enzymgranulat wies eine Proteaseaktivität von 145 600 PE/g auf.The hole diameter of the perforated plate of the extruder was 0.8 mm. The ratio of length to thickness of the granules was 1. After rounding and drying the granules in a fluidized bed dryer, the particles with particle sizes smaller than 0.4 mm and larger than 1.6 mm were sieved. The grain fraction between 0.4 mm and 1.6 mm was in a ball coater with Turbojet system from Hüttlin with a coating layer coated, a melt of 70% by weight technical stearyl alcohol, 6% by weight 40 times ethoxylated tallow fatty alcohol and 24% by weight titanium dioxide being used. The enzyme granulate containing silver protective agent obtained had a protease activity of 145,600 PE / g.
Es wurde in einer Menge von 1,1 Gew-% in ein maschinelles Geschirrspülmittel gemäß der deutschen Patentanmeldung 195 18 693.1 eingearbeitet, das 45 Gew.-% Trinatriumcitrat- Dihydrat, 32,15 Gew.-% Natriumhydrogencarbonat, 5 Gew.-% Natriumcarbonat, 3 Gew.- % Niotensid, 1 Gew.-% Amylasegranulat, 12 Gew.-% Natriumpercarbonat und 0,75 Gew.-% Isocyanursäure, jeweils bezogen auf fertiges Mittel, enthielt. Das Mittel wurde wie in der genannten Anmeldung beschrieben gestestet und im Hinblick auf seine silberschützende Wirkung bewertet. Es erreichte wie das Mittel, in das Enzym und Cystin nicht zusammen in einem Korn eingearbeitet waren, die Note 1,0 (kaum verfärbte Ober¬ fläche). It was incorporated in an amount of 1.1% by weight in a machine dishwashing detergent according to German patent application 195 18 693.1, the 45% by weight trisodium citrate dihydrate, 32.15% by weight sodium hydrogen carbonate, 5% by weight sodium carbonate , 3% by weight nonionic surfactant, 1% by weight amylase granules, 12% by weight sodium percarbonate and 0.75% by weight isocyanuric acid, each based on the finished agent. The agent was tested as described in the aforementioned application and evaluated with regard to its silver protective effect. Like the agent in which the enzyme and cystine were not incorporated together in one grain, it achieved a rating of 1.0 (hardly discolored surface).

Claims

Patentansprfiche Claims
1. Für die Einarbeitung in insbesondere teilchenfbrmige Reinigungsmittel geeignetes sil- berkorrosionsinhibitorhaltiges Enzymgranulat, dadurch gekennzeichnet, daß es Enzym, anorganisches und/oder organisches Trägermaterial für das Enzym und Silberkorro¬ sionsinhibitor sowie gegebenenfalls Granulierhilfsmittel in inniger Abmischung enthält.1. Enzyme granules containing silver corrosion inhibitor which are suitable for incorporation into particulate cleaning agents in particular, characterized in that they contain an enzyme, inorganic and / or organic carrier material for the enzyme and silver corrosion inhibitor and optionally granulation aids in intimate mixture.
2. Enzymgranulat nach Anspruch 1, dadurch gekennzeichnet, daß der Silberkorrosionsin¬ hibitor aus der Gruppe umfassend organische Disulfide, zweiwertige Phenole, dreiwer¬ tige Phenole sowie Mangan-, Titan-, Zirkonium-, Hafnium-, Vanadium-, Cobalt- öder Cersalze und/oder -komplexe, in denen die genannten Metalle in einer der Oxidations¬ stufen π, HI, IV, V oder VI vorliegen, ausgewählt wird.2. Enzyme granules according to claim 1, characterized in that the Silberkorrosionin¬ inhibitor from the group comprising organic disulfides, dihydric phenols, trivalent phenols and manganese, titanium, zirconium, hafnium, vanadium, cobalt or cerium salts and / or complexes in which the metals mentioned are present in one of the oxidation states π, HI, IV, V or VI.
3. Enzymgranulat nach Anspruch 1 oder 2, dadurch gekennzeichnet, daß der Silberkorro¬ sionsinhibitor Cystin, Hydrochinon, Brenzkatechin, Phloroglucin, Gallussäure, Hydroxyhydrochinon, Pyrogallol, MnSO4, V2O5, V2O4, VO2, TiOSO4, K2TiF6, K2ZrF6, CoSO4, Co(NO3)2 und/oder Ce(NO3)3 ist.3. Enzyme granules according to claim 1 or 2, characterized in that the Silberkorro¬ sionsinhibitor cystine, hydroquinone, pyrocatechol, phloroglucin, gallic acid, hydroxyhydroquinone, pyrogallol, MnSO 4 , V 2 O 5 , V 2 O 4 , VO 2 , TiOSO 4 , K 2 is TiF 6 , K 2 ZrF 6 , CoSO 4 , Co (NO 3 ) 2 and / or Ce (NO 3 ) 3 .
4. Enzymgranulat nach einem der Ansprüche 1 bis 3, dadurch gekennzeichnet, daß es 0,5 Gew.-% bis 40 Gew.-%, insbesondere 1 Gew.-% bis 30 Gew.-% enzymatisches Protein, 30 Gew.-% bis 95 Gew.-%, insbesondere 40 Gew.-% bis 80 Gew.-% Träger¬ material für das Enzym, gegebenenfalls 3 Gew.-% bis 12 Gew.-% Wasser und 0,5 Gew.-% bis 50 Gew.-%, insbesondere 5 Gew.-% bis 30 Gew.-% Silberkorrosions¬ inhibitor enthält.4. Enzyme granules according to one of claims 1 to 3, characterized in that it contains 0.5% by weight to 40% by weight, in particular 1% by weight to 30% by weight, of enzymatic protein, 30% by weight up to 95% by weight, in particular 40% by weight to 80% by weight, of carrier material for the enzyme, optionally 3% by weight to 12% by weight of water and 0.5% by weight to 50% by weight .-%, in particular 5 wt .-% to 30 wt .-% silver corrosion inhibitor contains.
5. Enzymgranulat nach einem der Ansprüche 1 bis 4, dadurch gekennzeichnet, daß es eine gleichmäßige äußere Umhüllungsschicht eines Überzugssystems aufweist, das 10 Gew.-% bis 30 Gew.-% feinteiliges anorganisches Pigment, 45 Gew.-% bis 80 Gew.-% eines Alkohols oder Alkoholgemisches mit einem Schmelzpunkt im Be¬ reich von 35 °C bis 75 °C, bis zu 15 Gew.-% Emulgator für den Alkohol, bis zu 5 Gew.-% Dispergiermittel für das Pigment und bis zu 5 Gew.-% Wasser enthält. 5. Enzyme granules according to one of claims 1 to 4, characterized in that it has a uniform outer coating layer of a coating system which 10 wt .-% to 30 wt .-% of finely divided inorganic pigment, 45 wt .-% to 80 wt .-% % of an alcohol or alcohol mixture with a melting point in the range from 35 ° C. to 75 ° C., up to 15% by weight emulsifier for the alcohol, up to 5% by weight dispersant for the pigment and up to 5% by weight. -% contains water.
6. Enzymgranulat nach einem der Ansprüche 1 bis 4, dadurch gekennzeichnet, daß es eine gleichmäßige äußere Umhüllungsschicht eines Überzugssystems aus mindestens 25 Gew.-% eines Silberkorrosionsinhibitors, insbesondere eines mit dem im Enzymkern enthaltenen Silberkorrosionsinhibitor nicht identischen Silberkorrosionsinhibitors, bis zu 30 Gew.-%, insbesondere 5 Gew.-% bis 25 Gew.-% feinteiligem anorganischem Pigment, 5 Gew.-% bis 75 Gew.-% bei Raumtemperatur festem Alkohol mit einem Schmelzpunkt im Bereich von 35 °C bis 75 °C, bis zu 10 Gew.-%, insbesondere 1 Gew.-% bis 5 Gew.-% Emulgator für den Alkohol, bis zu 5 Gew.-%, insbesondere 0,2 Gew.-% bis 3 Gew.-% Dispergiermittel für das anorganische Pigment beziehungs¬ weise den Silberkorrosionsinhibitor und bis zu 7 Gew.-% Wasser aufweist.6. Enzyme granules according to one of claims 1 to 4, characterized in that it has a uniform outer coating layer of a coating system composed of at least 25% by weight of a silver corrosion inhibitor, in particular a silver corrosion inhibitor which is not identical to the silver corrosion inhibitor contained in the enzyme core, up to 30% by weight. %, in particular 5% by weight to 25% by weight of finely divided inorganic pigment, 5% by weight to 75% by weight of alcohol which is solid at room temperature and has a melting point in the range from 35 ° C. to 75 ° C., up to 10 % By weight, in particular 1% by weight to 5% by weight, of emulsifier for the alcohol, up to 5% by weight, in particular 0.2% by weight to 3% by weight of dispersant for the inorganic pigment ¬ as the silver corrosion inhibitor and up to 7 wt .-% water.
7. Enzymgranulat nach Anspruch 5 oder 6, dadurch gekennzeichnet, daß der Alkohol in der Umhüllungsschicht ein primärer linearer Alkohol mit 14 bis 22 C-Atomen oder ein Gemisch aus diesen ist, und/oder daß die Umhüllungsschicht als anorganisches Pigment Titandioxid, Zinkoxid, Kreide und/oder Calciumcarbonat enthält.7. enzyme granules according to claim 5 or 6, characterized in that the alcohol in the coating layer is a primary linear alcohol having 14 to 22 carbon atoms or a mixture of these, and / or that the coating layer as an inorganic pigment titanium dioxide, zinc oxide, chalk and / or contains calcium carbonate.
8. Enzymgranulat nach einem der Ansprüche 1 bis 7, dadurch gekennzeichnet, daß es Protease, Amylase, Pullulanase, Lipase, Cutinase, Cellulase, Hemicellulase, Oxidase und/oder Peroxidase enthält.8. Enzyme granules according to one of claims 1 to 7, characterized in that it contains protease, amylase, pullulanase, lipase, cutinase, cellulase, hemicellulase, oxidase and / or peroxidase.
9. Enzymgranulat nach einem der Ansprüche 1 bis 8, dadurch gekennzeichnet, daß das Enzym Protease und der Silberkorrosionsinhibitor MnSO4 ist.9. enzyme granulate according to one of claims 1 to 8, characterized in that the enzyme protease and the silver corrosion inhibitor is MnSO 4 .
10. Enzymgranulat nach einem der Ansprüche 1 bis 8, dadurch gekennzeichnet, daß das Enzym Protease und der Silberkorrosionsinhibitor Cystin ist.10. Enzyme granules according to one of claims 1 to 8, characterized in that the enzyme protease and the silver corrosion inhibitor is cystine.
11. Enzymgranulat nach einem der Ansprüche 1 bis 8, dadurch gekennzeichnet, daß das Enzym Amylase und der Silberkorrosionsinhibitor Cystin ist11. Enzyme granules according to one of claims 1 to 8, characterized in that the enzyme is amylase and the silver corrosion inhibitor is cystine
12. Enzymgranulat nach einem der Ansprüche 1 bis 10, dadurch gekennzeichnet, daß es Protease mit einer Aktivität von 50 000 PE bis 350 000 PE, insbesondere 100 000 PE bis 300 000 PE, pro Gramm Enzymgranulat enthält. 12. Enzyme granules according to one of claims 1 to 10, characterized in that it contains protease with an activity of 50,000 PE to 350,000 PE, in particular 100,000 PE to 300,000 PE, per gram of enzyme granules.
13. Verfahren zur Herstellung von silberkorrosionsinhibitorhaltigen Enzymgranulaten durch Vermischen einer wäßrigen, das Enzym enthaltenden Flüssigkeit, die gegebenen¬ falls eine von unlöslichen Bestandteilen befreite und aufkonzentrierte Fermentations¬ brühe sein kann, mit anorganischem und/oder organischem Trägermaterial und dem Sil¬ berkorrosionsinhibitor, anschließende Extrusion der so erhaltenen Mischung durch eine Lochplatte mit anschließendem Schneidegerät, gegebenenfalls Sphäronisierung des Extrudats in einem Rondiergerät sowie Trocknung, und gegebenenfalls Aufbringen ei¬ nes gewünschtenfalls Farbstoff und/oder Pigment enthaltenden Überzugs.13. Process for the preparation of enzyme granules containing silver corrosion inhibitor by mixing an aqueous liquid containing the enzyme, which can optionally be a fermentation broth freed from insoluble constituents and concentrated, with inorganic and / or organic carrier material and the silver corrosion inhibitor, followed by extrusion the mixture thus obtained through a perforated plate with subsequent cutting device, optionally spheronization of the extrudate in a rounding device and drying, and optionally applying a coating optionally containing dye and / or pigment.
14. Verfahren nach Anspruch 13, dadurch gekennzeichnet, daß der Silberkorrosionsinhibi¬ tor aus der Gruppe umfassend organische Disulfide, zweiwertige Phenole, dreiwertige Phenole, Mangan-, Titan-, Zirkonium-, Hafnium-, Vanadium-, Cobalt- oder Cersalze und/oder -komplexe, in denen die genannten Metalle in einer der Oxidationsstufen Q, QI, IV, V oder VI vorliegen, ausgewählt wird.14. The method according to claim 13, characterized in that the silver corrosion inhibitor from the group comprising organic disulfides, dihydric phenols, trihydric phenols, manganese, titanium, zirconium, hafnium, vanadium, cobalt or cerium salts and / or complexes in which the metals mentioned are present in one of the oxidation states Q, QI, IV, V or VI.
15. Verfahren nach Anspruch 13 oder 14, dadurch gekennzeichnet, daß als quellfähiges Trägermaterial für das Enzym Cellulose, Maltodextrose, Saccharose, Invertzucker, Glukose oder deren Gemische, insbesondere ein Gemisch aus pulverfbrmiger Cellulose und Saccharose, eingesetzt wird, und als weitere Trägermaterialien Stärken, Getreide¬ mehle, Celluloseether, Alkalialumosilikat, insbesondere Zeolith, Schichtsilikat, insbe¬ sondere Bentonit oder Smectit, wasserlösliche anorganische oder organische Salze, insbesondere Alkalichlorid, Alkalisulfat, Alkalicarbonat oder Alkaliacetat, eingesetzt werden.15. The method according to claim 13 or 14, characterized in that the swellable carrier material for the enzyme cellulose, maltodextrose, sucrose, invert sugar, glucose or mixtures thereof, in particular a mixture of powdery cellulose and sucrose, is used, and starches as further carrier materials, Cereal flours, cellulose ethers, alkali alumosilicate, in particular zeolite, layered silicate, in particular bentonite or smectite, water-soluble inorganic or organic salts, in particular alkali metal chloride, alkali metal sulfate, alkali metal carbonate or alkali metal acetate, can be used.
16. Verfahren nach Anspruch 15, dadurch gekennzeichnet, daß das Trägermaterial Stärke in Mengen von 20 Gew.-% bis 80 Gew.-%, insbesondere von 25 Gew.-% bis 75 Gew.- %, und Getreidemehl in Mengen von 5 Gew.-% bis 35 Gew.-%, insbesondere von 10 Gew.-% bis 25 Gew. -% jeweils bezogen auf gesamtes Trägermaterial, enthält.16. The method according to claim 15, characterized in that the carrier material starch in amounts of 20 wt .-% to 80 wt .-%, in particular from 25 wt .-% to 75 wt .-%, and cereal flour in amounts of 5 wt % to 35% by weight, in particular from 10% by weight to 25% by weight, based in each case on the entire carrier material.
17. Verfahren nach einem der Ansprüche 13 bis 16, dadurch gekennzeichnet, daß der Durchmesser der Bohrungen in der Lochplatte 0,7 mm bis 1,6 mm, insbesondere 0,8 mm bis 1,4 mm beträgt. 17. The method according to any one of claims 13 to 16, characterized in that the diameter of the holes in the perforated plate is 0.7 mm to 1.6 mm, in particular 0.8 mm to 1.4 mm.
18. Verfahren nach einem der Ansprüche 13 bis 17, dadurch gekennzeichnet, daß man einen durch Extrusion hergestellten silberkorrosionsinhibitorhaltigen Enzymkern mit einem teilchenformig konfektioniertem zweiten Enzym und gegebenenfalls weiteren teilchenformig konfektionierten Enzymen unter Agglomerationsbedingungen vermischt, wobei die mittlere Teilchengröße des das erste Enzym enthaltenden Extrudatkerns ins¬ besondere das 1,1- bis 3-fache derjenigen des zweiten oder weiteren teilchenformig konfektionierten Enzyms beträgt.18. The method according to any one of claims 13 to 17, characterized in that an enzyme core prepared by extrusion containing silver corrosion inhibitor is mixed with a particulate assembled second enzyme and optionally further particulate assembled enzymes under agglomeration conditions, the mean particle size of the extrudate core containing the first enzyme ins¬ especially 1.1 to 3 times that of the second or further particulate enzyme.
19. Verfahren nach Anspruch 18, dadurch gekennzeichnet, daß das Enzym im Extrudat- kern Protease und das in den separat hergestellten, kleineren Teilchen, welche an das Extrudat agglomerieren, enthaltene Enzym Amylase, Lipase, Cellulase und/oder Oxida¬ se ist.19. The method according to claim 18, characterized in that the enzyme in the extrudate core protease and the enzyme contained in the separately produced, smaller particles which agglomerate to the extrudate, is amylase, lipase, cellulase and / or Oxida¬ se.
20. Verwendung eines Enzymgranulats gemäß einem der Ansprüche 1 bis 12 oder eines nach einem Verfahren gemäß einem der Ansprüche 13 bis 19 hergestellten Enzymgra- nulats zur Herstellung fester, insbesondere teilchenformiger Reinigungsmittel.20. Use of an enzyme granulate according to one of claims 1 to 12 or of an enzyme granulate produced by a method according to one of claims 13 to 19 for the production of solid, in particular particulate detergents.
21. Niederalkalisches Mittel zum maschinellen Reinigen von Geschirr, enthaltend Enzym, Silberkorrosionsinhibitor, 15 Gew.-% bis 60 Gew.-%, insbesondere 30 Gew.-% bis 50 Gew.-% wasserlösliche Builderkomponente, 5 Gew.-% bis 25 Gew.-%, insbeson¬ dere 10 Gew.-% bis 15 Gew.-% Bleichmittel auf Sauerstoffbasis, .1 Gew.-% bis 10 Gew.-%, insbesondere 2 Gew.-% bis 6 Gew.-% Bleichaktivator, dadurch gekenn¬ zeichnet, daß es 0,1 Gew.-% bis 10 Gew.-%, insbesondere 0,5 Gew.-% bis 5 Gew.-% Enzymgranulat enthält, welches Enzym, anorganisches und/oder organisches Träger¬ material für das Enzym und Silberkorrosionsschutzmittel sowie gegebenenfalls Granu¬ lierhilfsmittel in inniger Abmischung enthält. 21. Low-alkaline agent for machine cleaning of dishes, containing enzyme, silver corrosion inhibitor, 15% by weight to 60% by weight, in particular 30% by weight to 50% by weight of water-soluble builder component, 5% by weight to 25% by weight .-%, in particular 10 wt .-% to 15 wt .-% oxygen-based bleach, .1 wt .-% to 10 wt .-%, in particular 2 wt .-% to 6 wt .-% bleach activator, thereby gekenn¬ characterized that it contains 0.1 wt .-% to 10 wt .-%, in particular 0.5 wt .-% to 5 wt .-% enzyme granules, which enzyme, inorganic and / or organic carrier material for the Enzyme and silver corrosion inhibitor and optionally pelletizing agent in intimate mixture contains.
EP96920771A 1995-06-12 1996-06-03 Enzyme granulate containing anti-corrosion agents for silver Withdrawn EP0870007A1 (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
DE19521371 1995-06-12
DE1995121371 DE19521371A1 (en) 1995-06-12 1995-06-12 Enzyme granules containing silver corrosion inhibitor
PCT/EP1996/002386 WO1996041860A1 (en) 1995-06-12 1996-06-03 Enzyme granulate containing anti-corrosion agents for silver

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EP0870007A1 true EP0870007A1 (en) 1998-10-14

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US6204236B1 (en) 1996-06-01 2001-03-20 Genencor International, Inc. Enzyme granulates comprising an enzyme and an organic disulfide core
DE19622131A1 (en) * 1996-06-01 1997-12-04 Solvay Enzymes Gmbh & Co Kg New enzyme granules
EP1889904A3 (en) * 1999-10-01 2008-07-09 Novozymes A/S Enzyme granulate
DE10258869A1 (en) * 2002-12-17 2004-07-15 Henkel Kgaa Silver protection for automatic dishwashing
EP1571198A1 (en) * 2004-03-02 2005-09-07 Dalli-Werke GmbH & Co. KG. Polymer bound manganese compounds in cleaning compositions
DE102015217816A1 (en) 2015-09-17 2017-03-23 Henkel Ag & Co. Kgaa Use of highly concentrated enzyme granules to increase the storage stability of enzymes

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Publication number Priority date Publication date Assignee Title
BE792940A (en) * 1971-12-21 1973-06-18 Unilever Nv ENZYMATIC DETERGENT COMPOSITIONS
US5167854A (en) * 1985-08-21 1992-12-01 The Clorox Company Encapsulated enzyme in dry bleach composition
DE4041752A1 (en) * 1990-12-24 1992-06-25 Henkel Kgaa ENZYME PREPARATION FOR WASHING AND CLEANING AGENTS
DE4344215A1 (en) * 1993-12-23 1995-06-29 Cognis Bio Umwelt Silver corrosion inhibitor-containing enzyme preparation

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WO1996041860A1 (en) 1996-12-27

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