Classifications

• • A—HUMAN NECESSITIES
  • A47—FURNITURE; DOMESTIC ARTICLES OR APPLIANCES; COFFEE MILLS; SPICE MILLS; SUCTION CLEANERS IN GENERAL
  • A47L—DOMESTIC WASHING OR CLEANING; SUCTION CLEANERS IN GENERAL
  • A47L15/00—Washing or rinsing machines for crockery or tableware
  • A47L15/0002—Washing processes, i.e. machine working principles characterised by phases or operational steps
• • A—HUMAN NECESSITIES
  • A47—FURNITURE; DOMESTIC ARTICLES OR APPLIANCES; COFFEE MILLS; SPICE MILLS; SUCTION CLEANERS IN GENERAL
  • A47L—DOMESTIC WASHING OR CLEANING; SUCTION CLEANERS IN GENERAL
  • A47L15/00—Washing or rinsing machines for crockery or tableware
  • A47L15/42—Details
  • A47L15/4236—Arrangements to sterilize or disinfect dishes or washing liquids
  • A47L15/4238—Arrangements to sterilize or disinfect dishes or washing liquids by using electrolytic cells
• • A—HUMAN NECESSITIES
  • A47—FURNITURE; DOMESTIC ARTICLES OR APPLIANCES; COFFEE MILLS; SPICE MILLS; SUCTION CLEANERS IN GENERAL
  • A47L—DOMESTIC WASHING OR CLEANING; SUCTION CLEANERS IN GENERAL
  • A47L2601/00—Washing methods characterised by the use of a particular treatment
  • A47L2601/06—Electrolysed water

Definitions

• the invention relates to a process for bleaching kitchen preservatives in a dishwasher, and to the combination of a dishwasher with an electrolysis cell located outside the dishwasher in the supply line or with a battery-operated electrolysis cell located in the washing compartment.
• a dishwasher For bleaching kitchen utensils such as crockery and cutlery, detergents containing bleaches and / or bleach activators (bleach precursors) are commonly used to remove various types of stains, particularly tea and coffee stains, from the kitchenware to be cleaned.
• the "actual" bleaching agent for example singlet oxygen, is first formed in situ from the bleaching agents used and / or bleach activators.
• bleaching agents are hydrogen peroxide sources such as sodium percarbonate and sodium perborate, which form hydrogen peroxide in the presence of water, which in turn decomposes at temperatures above 60 ° C to water and singlet oxygen.
• hydrogen peroxide sources When using hydrogen peroxide sources, the bleaching effect only occurs at temperatures above 60 ° C.
• bleach activators are acyl derivatives such as tetraacetylethylenediamine (TAED) and sodium p-nonanoyloxybenzenesulfonate (NOBS).
• TAED tetraacetylethylenediamine
• NOBS sodium p-nonanoyloxybenzenesulfonate
• the acyl derivative bleach activators are used in conjunction with a hydrogen peroxide source. Upon release of the hydrogen peroxide from the source of hydrogen peroxide, the acyl derivative bleach activators react with hydrogen peroxide to form peroxycarboxylic acids.
• the peroxycarboxylic acids usually decompose even at room temperature to form the carboxylic acid and singlet oxygen.
• hydrogen peroxide is only released at higher temperatures; for example, sodium percarbonate only forms hydrogen peroxide at temperatures above 50 ° C. in the presence of water.
• the combination of acyl derivative bleach activator / hydrogen peroxide source depending on the hydrogen peroxide source
• Hydrogen peroxide and many peroxycarboxylic acids, for example peroxyacetic acid, are unstable, and thus not storable, and therefore can not be added directly to the dishwashing detergent.
• US 6,387,238 describes a process for preparing an antimicrobial solution containing peroxyacetic acid. This process involves the electrolytic production of hydrogen peroxide, peroxide ions or peroxide radicals and the reaction of these species with a Acetyl donor to form peroxyacetic acid.
• Example 1 describes the electrolytic (current strength: 5 A, current density: 100 mA / cm 2 , voltage: 10 V) Production of peroxyacetic acid.
• WO 2006/1 17201 describes a method for cleaning, sterilizing and disinfecting utensils and other kitchen aids by means of a washing liquid, wherein by direct application of electric current to an arranged in the washing liquid electrode serving as a diamond and / or lead-tin electrode OH radicals are generated in the washing liquid, which makes it possible to clean, disinfect and disinfect the eating utensils and other kitchen aids.
• US 2002/023847 describes a process for the preparation of a cleaning solution by means of electrolysis of water and an apparatus for cleaning and sterilizing objects such as dishes and clothing.
• the apparatus comprises, for example, an electrolysis chamber having a ion exchange membrane which separates the anode space from the cathode space.
• the cathode compartment contains tap water
• the anode compartment contains salt water.
• an aqueous solution of sodium hydroxide is formed in the cathode compartment
• an aqueous solution of HOCl is formed in the anode compartment.
• the aqueous solution of sodium hydroxide is pumped out of the cathode compartment and the objects to be cleaned are sprayed with it.
• JP 2003/21 1 104 A describes a washing station which has a washing water treatment unit comprising a cathode and an anode, wherein the surface of at least one of the electrodes has conductive diamond.
• a washing station is a dishwasher (tableware scrubber).
• Example 3 describes the formation of an aqueous persulfate solution by electrolysis (5 A, 120 cm 2 , 15 min, 14 V) of a 0.6% aqueous sodium sulfate solution using WO 2009/067838 describes a method for cleaning, sanitizing, disinfecting and odor neutralizing laundry, textiles, dishes, floor surfaces and vehicles with electrolysed cold or warm water by means of oxidative radicals generated by boron-doped diamond electrodes Purpose required cleaning intensities by means of oxidative Radiake can only be achieved with the help of diamond electrodes with 4 volt overvoltage.
• EP 1 944 403 describes a process for working up the washing water of a cleaning device, for example a washing machine, and for reuse of the worked-up washing water in the cleaning device, wherein the method, inter alia, provides a step in which the wash water to be worked up is treated electrochemically.
• organic components of the wash water to be worked up z.
• hypochlorous acid (HOCl) or others decomposes active oxygen species.
• diamond electrodes may be used, and a high voltage is applied to form highly concentrated ozone.
• US 2003/0414202 describes the production of electrolytic water by the electrolysis of an alkaline electrolyte solution, wherein the electrolytic water can be taken for cleaning and disinfecting.
• the alkaline electrolyte is a mixture of at least one electrolyte selected from the group consisting of sodium carbonate, potassium carbonate, phosphoric sodium carbonate and sodium hypochlorite and another electrolyte selected from the group consisting of sodium chloride, potassium chloride, sodium bromide and potassium bromide.
• As the anode nickel ferrite can be used.
• the invention can be used in many applications, such as cleaning and disinfecting hot water in public baths.
• DE 103 36 588 A1 describes a process for the removal / discoloration of colored substances / residues in liquids and of surfaces, in particular in dishwashers and in washing machines.
• the liquid continuously flows through channels between electrodes in the circuit.
• the colored molecules are anodized directly at the electrode surface.
• "active" oxygen and “active” chlorine are formed on the electrode surfaces, the accumulation of which also causes removal / discoloration of colored substances / residues in the liquid and surfaces.
• anode for example, an anode of titanium having a layer of titanium oxide can be used.
• DE 10 2006 037 905 describes a dishwasher comprising an electrolysis cell for producing bleaching agents from the regenerating salt of a water softener.
• oxidatively active substances in particular chlorine and sodium chlorite solution or potassium hypochlorite solution
• bleaching agents in particular chlorine and sodium chlorite solution or potassium hypochlorite solution
• By-products are hydrogen gas and oxygen gas.
• the electrodes are preferably made of corrosion-resistant materials also with catalytic coating, B. electrodes of titanium substrate with oxidative coating of noble metal oxides and precious metal dopants. In addition, however, other electrode materials such as conductive diamond, platinum, tin oxide and stainless steels can be used.
• the object of the present invention was to provide a method for bleaching kitchen aids in a dishwasher, which achieves excellent bleaching results even at temperatures of less than 45 ° C.
• the inventive method should also technically feasible (no storage of unstable bleaching agents such as hydrogen peroxide or peroxycarboxylic acids) and economically (little power consumption), as well as gentle on the dishwasher (no corrosion) and kitchen aids (no unwanted discoloration).
• the method of bleaching kitchen aids in a dishwashing machine of the present invention includes the step of in situ activation of a bleach activator by means of a reactive oxygen species, wherein the reactive oxygen species is generated in situ in the dishwasher by electrolysis of an aqueous solution.
• Dishwasher includes all types of dishwashers, that is, both dishwashers for private household (household dishwashers) and commercially applicable dishwashers (industrial and commercial dishwashers).
• the reactive oxygen species is usually a reactive oxygen species having at least one oxygen atom with the oxidation number -1.
• Examples of reactive oxygen species which have at least one oxygen atom with the oxidation number -1 are hydrogen peroxide, hydrogen peroxide anions, perhydroxyl radicals, hydroxyl radicals, peroxide anions and ozone.
• the reactive oxygen species is selected from the group consisting of hydrogen peroxide, hydrogen peroxide anions, perhydroxyl radicals and hydroxyl radicals.
• the reactive oxygen species is particularly preferably selected from the group consisting of hydrogen peroxide, hydrogen peroxide anions and perhydroxyl radicals.
• the reactive oxygen species is preferably generated by electrolysis of the water contained in the aqueous solution.
• the electrolysis may be carried out in an electrolytic cell containing at least one anode / cathode pair.
• the electrolytic cell may include an anode / cathode pair or a plurality of serially connected anode / cathode pairs.
• the electrolysis cell preferably contains a plurality of serially connected anode / cathode pairs.
• the circuit of the anode / cathode pairs can be monopolar or bipolar. A bipolar circuit is preferred.
• the anode may contain the following materials: carbon for example graphite, glassy carbon and electric current conductive diamond, precious metals for example platinum and gold, me- talloxides, for example iridium oxide, chromium oxide, lead oxide, palladium oxide and ruthenium oxide, or mixed metal oxides.
• the anode contains graphite, electric current conductive diamond or platinum
• the anode contains materials with which a high oxygen overvoltage can be achieved, for example electric current-conducting diamond or platinum.
• the anode most preferably contains electrical current conductive diamond.
• Electric current conductive diamond is diamond which is doped with impurities so that the impurity doped with impurities directs the electric current. Suitable foreign atoms are, for example, boron or nitrogen.
• the anode is an anode containing electric current conductive diamond, wherein the electric current conducting diamond is a boron-doped diamond.
• Anodes containing electric current conductive diamond usually contain a support material, and the electric current conductive diamond.
• Possible support materials are niobium, silicon, tungsten, titanium, silicon carbide, tantalum and graphite, and also ceramic support materials such as titanium suboxide.
• Preferred support materials are niobium, titanium and silicon.
• a particularly preferred carrier material is niobium
• the cathode may contain the following materials: carbon for example graphite, glassy carbon and electric current conductive diamond, metals for example iron and nickel, steel for example stainless steel, or precious metals for example platinum.
• the cathode most preferably contains electrical current conductive diamond or steel.
• the cathode is a cathode containing electric current conducting diamond, wherein the electric current conducting diamond is a boron-doped diamond.
• Cathodes containing electric current conductive diamond usually contain a support material, and the electric current conductive diamond.
• Possible support materials are niobium, silicon, tungsten, titanium, silicon carbide, tantalum and graphite, and also ceramic support materials such as titanium suboxide.
• Preferred support materials are niobium, titanium and silicon.
• a particularly preferred carrier material is niobium Anodes or cathodes containing electrical current-conducting diamond can be produced by the CVD ("chemical vapor deposition") method Such diamond electrodes are commercially available, for example from Condias GmbH or Adamant Technologies.
• Anodes or cathodes containing electric current conductive diamond can also be made by the high temperature high pressure (HTHP) process, whereby industrial diamond powder is mechanically introduced into the surface of a carrier sheet Diamond Electrode Production GmbH.
• HTHP high temperature high pressure
• the anode contains boron-doped diamond, and the dishwasher housing containing steel, preferably stainless steel, acts as a cathode.
• the dishwasher is thus part of the electrolysis cell.
• the dishwasher housing is preferably not part of the electrolysis cell.
• both the anode and the cathode contain boron-doped diamond.
• This embodiment has the advantage that the polarity of the electrodes can be reversed and any deposits on the electrodes can be removed. For example, the electrode polarity can be changed every 5 seconds to every 200 minutes, or between each rinse.
• the electrolysis cell preferably has an effective electrode surface area (electrode size) of 0.5 to 1000 cm 2 , preferably of 1 to 500 cm 2 and particularly preferably of 2 to 100 cm 2 .
• the effective electrode surface refers to the electrode surface of the anode or of the anodes, which comes into contact with the aqueous solution during the electrolysis and faces the cathode or the cathodes. If an anode is located between two cathodes (in series connection of several anode / cathode pairs), the effective electrode surface of the anode or of the anodes results from the sum of the electrode surfaces facing the cathodes.
• the electrodes are preferably of equal size so that the effective electrode surface remains the same when the electrode polarities are exchanged.
• the distance is preferably 0.1 to 20 mm, preferably 0.5 to 10 mm, particularly preferably 1 to 5 mm.
• the anode and the cathode are preferably not spatially separated, for example by a membrane.
• electrolysis cell electrolysis cell types known to those skilled in the art, such as divided or undivided flow cell, capillary gap cell or plate stack cell can be used.
• a particularly preferred electrolysis cell is the undivided flow cell.
• the electrolysis cell can either be a permanently installed component of the dishwasher or a separate component.
• the electrolysis cell is a permanently installed component of the dishwasher, then the electrolysis cell can be installed, for example, in the flooded area of the washing tub, preferably outside the washing space, or the electrolysis cell can be installed in the supply line within the dishwasher, or the electrolysis cell can be installed in a dishwashing machine. integrated in an additional water cycle within the dishwasher.
• a dishwasher which contains an electrolysis cell, wherein the electrolysis cell is integrated in an additional water cycle within the dishwasher, is also part of this invention.
• the electrolysis cell can be installed, for example, in the supply line outside the dishwasher, for example in the fresh water inlet between the tap and the dishwasher, or be used as a battery-powered electrolysis cell in the washing compartment.
• Dishwashers which are commercially available today, usually do not contain an electrolytic cell as a built-in component. Therefore, it is preferable that the electrolytic cell is used as a separate component. Particularly preferably, the electrolysis cell is a battery-operated electrolysis cell, which is used in the washing compartment of the dishwasher.
• a combination of a dishwasher with an outside of the dishwasher located in the supply line electrolysis cell is also part of this invention.
• a combination of a dishwasher with a battery-operated electrolysis cell located in the washing compartment is also part of this invention.
• the electrolysis is preferred at current densities based on the effective electrode surface in the range of 0.5 to 1000 mA / cm 2 , more preferably in the range of 1 to 500 mA / cm 2 , most preferably in the range of 10 to 200 mA / cm 2, and most preferably in the range of 50 to 100 mA cm 2 .
• the electrolysis is preferably carried out at currents of 0.02 to 30 A.
• a current strength in the range of 0.1 to 16 A is particularly preferred, and very particularly preferred is a current strength in the range of 0.1 to 10 A.
• the washing programs of a dishwasher usually contain a rinse and a rinse cycle.
• the rinse In the rinse, the items to be washed are cleaned, while the rinse cycle is used to remove the rinse water and to dry the items to be washed.
• the rinse may include multiple sub-rinses, for example one or more pre-rinses and one or more main rinses.
• the electrolysis may take place throughout the duration of the dishwasher program, but preferably the electrolysis takes place only at one or more time intervals during the dishwashing program.
• the electrolysis preferably takes place here in one or more time intervals before or during the rinse cycle.
• the time intervals in which the electrolysis takes place can be between 5 seconds and 120 minutes, preferably between 5 seconds and 60 minutes, more preferably between 1 minute and 30 minutes, and in particular between 5 minutes and 15 minutes.
• the electrolysis takes place at several intervals between 1 minute and 30 minutes, preferably between 5 minutes and 15 minutes, before or during the rinse cycle.
• the process according to the invention can be carried out at temperatures in the range from 10 to 95.degree. C., preferably in the range from 15 to 90.degree. C., more preferably in the range from 20 to 65.degree. C. and very particularly preferably in the range from 20 to 40.degree. for example, 30 ° C, to be performed.
• the process is preferably carried out at a temperature of up to 60 ° C., preferably up to 40 ° C., more preferably up to 30 ° C.
• the aqueous solution is an aqueous solution containing electrolytes, thus conducting the electric current.
• Examples of aqueous solutions that contain electrolytes and thus conduct electricity are aqueous solutions based on tap water.
• the aqueous solution may contain additives when carrying out the electrolysis.
• the additives can also be added to the aqueous solution during or after the electrolysis has been carried out.
• additives are the bleach activator, dishwashing detergent, rinse aid and regenerating salt.
• preferred additive is the bleach activator.
• Bleach activators are usually compounds which react with reactive oxygen species, in particular with hydrogen peroxide, hydrogen peroxide anions or perhydroxyl radicals, to peroxycarboxylic acids or peroxyimino acid. Both peroxycarboxylic acids and peroxyimino acid may decompose to form singlet oxygen.
• the bleach activators which react with hydrogen peroxide to form peroxycarboxylic acids are preferably acyl derivatives.
• the acyl radical of the acyl derivatives may have the formula: O
• R 1 is Ci-20-alkyl or C 6 -io-aryl, or
• L 1 is Ci-20-alkylene or C6-io-arylene.
• R 1 is C 1-10 -alkyl or phenyl, more preferably R 1 is C 1-3 -alkyl. Most preferably, R 1 is methyl.
• L 1 is phenylene or naphthylene, more preferably L 1 is phenylene.
• formula (2) has the following formula
• Acyl derivatives in which the acyl group has formula (1) are preferable to acyl derivatives in which the acyl group has formula (2).
• C 1-3 -alkyl are methyl, ethyl, n-propyl and isopropyl.
• Ci-10-alkyl may be unbranched or branched.
• Examples of C 1-10 -alkyl are methyl, ethyl, n-propyl, isopropyl, n-butyl, sec-butyl, isobutyl, ferf-butyl, n-pentyl, n-hexyl, n-heptyl, n-octyl, n- Nonyl and n-decyl, n-undecyl, n-dodecyl.
• Ci-20-alkyl may be unbranched or branched.
• C 1-20 -alkyl examples are methyl, ethyl, n-propyl, isopropyl, n-butyl, sec-butyl, isobutyl, fer-butyl, n-pentyl, n-hexyl, n-heptyl, n-octyl, n- Nonyl, n-decyl, n-undecyl, n-dodecyl, n-undecyl, n-dodecyl, n-tridecyl, n-tetradecyl, n-pentadecyl, n-hexadecyl, n-heptadecyl, n-octadecyl, n-nonadecyl and n-eicosyl (C20).
• C6-io-aryl may be phenyl or naphthyl.
• Ci-20-alkylene may be unbranched or branched.
• Examples of C 1 -20 -alkylene are methylene, ethylene, propylene, isopropylene, butylene, sec-butylene, isobutylene, ferf-butylene, pentylene, hexylene, heptylene, octylene, nonylene, decylene, undecylene, dodecylene, undecylene, dodecylene, Tri-decylene, tetradecylene, 2-decyldbutylene, pentadecylene, hexadecylene, heptadecylene, octadecylene, nonadecylene and eicosylene (C20).
• C6-io-arylene examples include phenylene and naphthylene.
• acyl derivative bleach activators are poly-O-acylated polyols, O-acylated phenol derivatives, carboxylic anhydrides, O-acylated hydroxylamines, O-acylated cyanuric acid derivatives, poly-N-acylated polyamines, N-acylated aniline derivatives, poly-N-acylated at least one nitrogen -containing heterocycles, N-acylated urea derivatives, N-acylated amides,
• N-acylated imides and N-acylated sulfonic acid amides.
• poly-O-acylated polyols are diacetylglycol and triacetin, as well as poly-O-acetylated sugar alcohols and sugars, for example hexaacetylsorbitol, hexaacetylmannitol, pentacetylglucose, tetraacetylxylose and octaacetyllactose, and tetraacetylgluconolactone.
• O-acylated phenol derivatives are sodium p-nonanoyloxybenzenesulfonate (NOBS), sodium p-isononanoyloxybenzenesulfonate, sodium p-benzoyloxybenzenesulfonate, sodium p-nonanoyloxybenzoate, and sodium p-decanoyloxybenzoate.
• NOBS sodium p-nonanoyloxybenzenesulfonate
• Na p-isononanoyloxybenzenesulfonate sodium p-benzoyloxybenzenesulfonate
• sodium p-nonanoyloxybenzoate sodium p-decanoyloxybenzoate
• carboxylic acid anhydrides examples include phthalic anhydride and benzoic anhydride.
• O-acylated hydroxylamines are 0-benzoyl-N, N-succinylhydroxylamine, O-acetyl- ⁇ , ⁇ -succinyl-hydroxylamine and ⁇ , ⁇ , ⁇ -triacetylhydroxylamine.
• O-acylated cyanuric acid derivatives are triacetylcyanuric acid and tribenzoylcyanuric acid.
• poly-N-acylated polyamines are tetraacetylmethylenediamine, tetraacetylethylenediamine (TAED) and tetraacetylhexylenediamine.
• N-acylated aniline derivative is N, N-diacetylaniline.
• poly-N-acylated at least one nitrogen-containing heterocycles are 1, 3-diacetyl-5,5-dimethylhydantoin, tetraacetylglucoluril, 1, 5-diacetyl-2,2-dioxo-hexahydro-1, 3,5-triazine, 1, 5-Diacetyl-2,4-dioxohexahydro-1,3,5-triazine, 1,4-diacetyl-2,5-diketopiperazine, 1,3-diacetyl-4,5-diacetoxyimidazoline and monoacetylmaleic hydrazide.
• An example of an N-acylated urea derivative is tetraacetylpropylenediurea.
• N-acylated amide is benzoyl-caprolactam.
• N-acylated imide is N-nonanoyl succinimide.
• N-acylated sulfonic acid amides are N-methyl-N-mesyl-acetamide, N-methyl-N-mesyl-benzamide, N, N'-dimethyl-N, N'-diacetylsulfurylamide and N, N'-diethyl-N, N'-dipropanoyl-sulfurylamide.
• Bleach activators which react with peroxyimino acid with hydrogen peroxide may be ammonium nitriles, for example N-methylmorpholinium acetonitrile hydrogen sulfate, trimethylammonium acetonitrile hydrogen sulfate.
• Bleach activators which react with hydrogen peroxide to form peroxycarboxylic acids are preferred.
• Particularly preferred bleach activators are acyl derivative bleach activators.
• Very particularly preferred bleach activators are poly-N-acylated polyamines.
• a particularly preferred bleach activator is tetraacetylethylenediamine (TAED).
• the concentration of the bleach activator in the aqueous solution may be 0.001 to 10% by weight, preferably 0.01 to 5% by weight, particularly preferably 0.02 to 1% by weight, based on the weight of the aqueous solution.
• the bleach activator may be part of the dishwashing detergent.
• the dishwashing detergent may contain the usual ingredients for a dishwashing detergent, for example water softeners, bleaches, bleach activators, bleach catalysts, bleach stabilizers, surfactants and enzymes.
• the dishwashing detergent may also contain foam inhibitors, corrosion inhibitors and fillers.
• water softeners examples include pentasodium triphosphate, sodium carbonate, sodium bicarbonate, soap, zeolites and complexing agents such as ethylenediaminetetraacetic acid (EDTA). Pentasodium triphosphate or zeolite are the preferred water softeners.
• bleaching agents are "oxygen-based” bleaching agents and "chlorine-based” bleaching agents.
• hydrogen peroxide sources are alkali metal perborates, for example sodium perborate, and alkali metal percarbonates, for example sodium percarbonate, alkali metal persulphates, for example potassium monopersulfate, alkali metal persilicates and alkali metal perphosphates.
• chlorine-based bleaching agent sodium hypochlorite.
• Oxygen-based bleaching agents are preferred, especially sodium perborate and sodium percarbonate. The most preferred bleaching agent is sodium percarbonate.
• bleach stabilizers are phosphonates.
• surfactants are anionic surfactants, for example, linear alkylbenzenesulfonates, secondary alkanesulfonates, fatty alcohol sulfates and methyl ester sulfates, and nonionic surfactants, for example, fatty alcohol polyglycol ethers and sugar surfactants.
• enzymes examples include amylases, lipases and proteases.
• foam inhibitors are silicone oils and paraffin oils.
• An example of a corrosion inhibitor is sodium metasilicate.
• An example of a filler is sodium sulfate.
• the regenerating salt is sodium chloride.
• Particularly preferred additives are water softeners, bleach activators, surfactants and enzymes.
• the pH of the aqueous solution is preferably in the range of 2 to 13, more preferably in the range of 3 to 12, and most preferably in the range of 6 to 1 1.
• a degree of soil removal for bleachable soils, for example tea of at least 20%, preferably at least 50%, is preferably achieved.
• the degree of soil removal is determined as follows:
• the determination is carried out by firstly staining a white melamine resin reference substrate under standardized conditions (using: DM 1 1 Tea Series 096, 2.4 cm ⁇ 3.9 cm) and, before and after carrying out the treatment with the aqueous solution of a reflection measurement at 460 nm. Dirt removal is determined from the remission values R before and after the method and the remission value of a white melamine resin reference substrate according to the following formula in%:
• the reflectance measurements are carried out with a Spectrophotometer Gretag Macbeth, type Spectrolino under the following conditions: observer angle 10 °, illuminant D65, UV filter.
• the process according to the invention is distinguished by the fact that it is outstandingly suitable for bleaching kitchen preservatives in a dishwashing machine, the process also having a very good bleaching effect even at temperatures of less than 45.degree.
• the inventive method is further technically feasible (no storage of unstable bleaching agents such as hydrogen peroxide or peroxycarboxylic) and economical (low power consumption), as well as the dishwasher (no corrosion) and kitchen aids (no unwanted discoloration).
• the method can show positive accompanying effects, such as decolorization of the aqueous solution, as well as disinfecting, cleaning and odor neutralization of the kitchen products to be bleached.
• Figure 1 shows the schematic representation of the experimental apparatus used in the examples.
• test substrates are made of melamine resin (DM 1 1 Tea Series 096, 2.4 cm x 3.9 cm).
• aqueous solutions are used:
• Aqueous solution A 700 g demineralized water, 10 g NaHCOs
• Aqueous solution B 700 g DI water, 10 g NaHCOs, 0.18 g TAED
• Aqueous solution C 700 g of DI water, 10 g NaHCOs, 0.18 g TAED, 0.32 g H 2 O 2 solution (30% H 2 O 2 in water)
• TAED is tetraacetylethylenediamine. Demineralised and desalinated water is demineralised water.
• the selected concentration of TAED in the aqueous solutions B and C corresponds to that of commercially available dishwashing detergents.
• the aqueous solutions A (V1), B (V2) and C (V3) are provided in the experimental apparatus.
• the test substrates are placed in the jacketed vessel so that they are completely immersed in and wetted by the aqueous solution.
• the aqueous solutions are pumped at 40 ° C without electrolysis for 30 minutes.
• the test substrates are removed from the test apparatus, rinsed thoroughly with deionised water, dried under exclusion of light.
• the aqueous solution B is provided in the experimental apparatus.
• the test substrate is placed in the jacketed vessel so that it is completely immersed in the aqueous solution and wetted by it.
• the aqueous solution B is pumped in the test apparatus at 40 ° C with electrolysis (1 .2 A) for 30 minutes.
• the test substrate is removed from the experimental apparatus, rinsed thoroughly with deionised water, dried under exclusion of light.
• the aqueous solution B is provided in the experimental apparatus.
• the test substrate is placed in the double-walled vessel so that it is completely immersed in the aqueous solution and wetted by it.
• the aqueous solution B is pumped in the test apparatus at 60 ° C with electrolysis (1.2 A) for 30 minutes.
• the test substrate is removed from the experimental apparatus, rinsed thoroughly with deionised water, dried under exclusion of light.
• the aqueous solution A is pumped in the test apparatus at 40 ° C with electrolysis (1 .2 A) for 10 minutes without test substrate.
• the power source is turned off.
• 0.18 g TAED and the test substrate are added and the resulting aqueous solution is circulated at 40 ° C for a further 30 minutes without current application.
• the test substrate is removed from the experimental apparatus, rinsed thoroughly with deionised water, dried under exclusion of light.
• the aqueous solution A is circulated in the test apparatus at 60 ° C with electrolysis (1.2 A) for 10 minutes without test substrate.
• the power source is turned off.
• 0.18 g TAED and the test substrate are added and the resulting aqueous solution is circulated at 60 ° C for a further 30 minutes without current application.
• the test substrate is removed from the experimental apparatus, rinsed thoroughly with deionised water, dried under exclusion of light.
• Dirt removal is determined by subjecting the melamine resin test substrate before and after treatment with the aqueous solution to a reflectance measurement at 460 nm.
• the soil removal was determined from the remission values R before and after the treatment and the remission value of a white reference substrate made of melamine resin according to the following formula in%:
• test substrates of Comparative Examples C1 to V3 and Examples 1 to 4 have the following degree of soil removal after treatment: Example Temperature [° C] Dirt removal [%]
• the pure washing effect of the aqueous solution A causes a dirt removal of 21% (V1).
• V2 The addition of TAED (V2) leads, as expected, only to a slight improvement in soil removal to 25%.
• the bleach precursor TAED is activated by the addition of H2O2 (V3), so that a dirt removal of 48% is achieved.
• Example 1 shows that at 40 ° C and the same amount of TAED with the inventive method, a higher soil removal (60%) can be achieved, as compared with the comparison method V3 (48%).
• Example 2 shows that the dirt removal by increasing the temperature increases to 60 ° C to 67%.
• Examples 3 and 4 show that it is also possible first to activate the aqueous solution electrolytically for 10 minutes and then to add TAED. It is thus possible to achieve a very good dirt removal with a lower current input.

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• 2012
  • 2012-09-04 CA CA2842396A patent/CA2842396A1/en not_active Abandoned
  • 2012-09-04 JP JP2014527695A patent/JP2014529455A/ja active Pending
  • 2012-09-04 RU RU2014113179/12A patent/RU2014113179A/ru not_active Application Discontinuation
  • 2012-09-04 WO PCT/EP2012/067220 patent/WO2013034548A1/de active Application Filing
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