WO2000015753A1 - Corps moules de lavage et de nettoyage contenant de l'alkyle benzene sulfonate - Google Patents

Corps moules de lavage et de nettoyage contenant de l'alkyle benzene sulfonate Download PDF

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Publication number
WO2000015753A1
WO2000015753A1 PCT/EP1999/006412 EP9906412W WO0015753A1 WO 2000015753 A1 WO2000015753 A1 WO 2000015753A1 EP 9906412 W EP9906412 W EP 9906412W WO 0015753 A1 WO0015753 A1 WO 0015753A1
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weight
alkylbenzenesulfonate
compounds
acid
detergent
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PCT/EP1999/006412
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German (de)
English (en)
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Andreas Lietzmann
Georg Assmann
Christian Block
Hans-Friedrich Kruse
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Henkel Kommanditgesellschaft Auf Aktien
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Publication of WO2000015753A1 publication Critical patent/WO2000015753A1/fr

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    • C—CHEMISTRY; METALLURGY
    • C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11D—DETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
    • C11D17/00—Detergent materials or soaps characterised by their shape or physical properties
    • C11D17/0047—Detergents in the form of bars or tablets
    • C11D17/0065—Solid detergents containing builders
    • C11D17/0073—Tablets
    • C—CHEMISTRY; METALLURGY
    • C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11D—DETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
    • C11D1/00—Detergent compositions based essentially on surface-active compounds; Use of these compounds as a detergent
    • C11D1/02—Anionic compounds
    • C11D1/12—Sulfonic acids or sulfuric acid esters; Salts thereof
    • C11D1/22—Sulfonic acids or sulfuric acid esters; Salts thereof derived from aromatic compounds

Definitions

  • the present invention is in the field of compact moldings which have washing and cleaning properties.
  • washing and cleaning agent shaped articles include, for example, detergent shaped articles for washing textiles, cleaning agent shaped articles for machine dishwashing or cleaning hard surfaces, bleaching agent shaped articles for use in washing machines or dishwashers, water softening shaped articles or stain tablets.
  • the invention relates to detergent tablets which are used for washing textiles in a household washing machine and are referred to briefly as detergent tablets.
  • Detergent tablets are widely described in the prior art and are becoming increasingly popular with consumers because of the simple dosage.
  • Tableted detergents and cleaning agents have a number of advantages over powder-form ones: They are easier to dose and handle and, thanks to their compact structure, have advantages in terms of storage and transport. Consequently, detergent tablets are also described comprehensively in the patent literature.
  • a problem that occurs again and again when using washing and cleaning active molded articles is the too slow disintegration and dissolving speed of the molded articles under application conditions.
  • the delayed disintegration of the molded article also has the disadvantage that conventional detergent and molded article articles cannot be washed in via the washing-in chamber of household washing machines, since the tablets do not disintegrate into secondary articles that are small enough to pass from the washing-in chamber into the washing drum to be washed in.
  • the washing performance of washable and cleaning-active molded articles is guaranteed by the use of surfactants, alkylbenzenesulfonates occupying an important position due to their high cleaning performance and large-scale availability.
  • One of the objects of the present invention was therefore to provide a detergent molded article in which the preparation of a surfactant alone causes it to disintegrate more quickly at a predetermined hardness.
  • Another object of the present invention was to make the incorporation form of the alkylbenzenesulfonate variable to such an extent that the form usually used in the production of detergent and cleaning agent cores of surfactant granules used can be used in varying amounts and a resulting quantity of surfactant can easily be compensated for via the premix to be tabletted, without adversely affecting the physical properties of the detergent tablets, in particular the hardness and disintegration time.
  • the incorporation form to be found should be so flexibly manageable that it can be introduced into the detergent tablets not only via the premix, but also via the surfactant granules, without resulting in negative properties of the molded articles during incorporation in this way.
  • the present invention relates to detergent tablets made of compressed, particulate detergents and cleaning agents which contain alkylbenzenesulfonate compounds with alkylbenzenesulfonate contents above 40% by weight, based on the compound.
  • alkylbenzenesulfonates as powerful anionic surfactants have been known since the 1930s. At that time, alkylbenzenes were produced by monochlorination of kogasin fractions and subsequent Friedel-Crafts alkylation, which were sulfonated with oleum and neutralized with sodium hydroxide solution.
  • propylene was tetramerized to branched ⁇ -dodecylene and the product was converted to tetrapropylene benzene via a Friedel-Crafts reaction using aluminum trichloride or hydrogen fluoride, which was subsequently sulfonated and neutralized.
  • Linear alkylbenzenesulfonates are made from linear alkylbenzenes, which in turn are accessible from linear olefms.
  • petroleum fractions with molecular sieves are separated on an industrial scale into the n-paraffins of the desired purity and dehydrogenated to the n-olefins, resulting in both ⁇ - and i-olefins.
  • the resulting olefins are then reacted with benzene in the presence of acidic catalysts to give the alkylbenzenes, the choice of Friedel-Crafts catalyst having an influence on the isomer distribution of the linear alkylbenzenes formed: when using aluminum trichloride, the content of the 2-phenyl isomers is in the mixture with the 3, 4, 5 and other isomers at approx. 30% by weight, however, if hydrogen fluoride is used as a catalyst, the 2-phenyl isomer content can be reduced to approx. 20% by weight .
  • alkylbenzenesulfonate compounds have alkylbenzenesulfonate contents above 50% by weight, preferably above 60% by weight and in particular above 70% by weight, based on the compound.
  • the alkylbenzenesulfonate compounds contain the alkali metal, preferably sodium salts of C 8 -i6-, preferably C 9 - ⁇ 3 - alkybenzenesulfonic acids which are derived from alkylbenzenes which have a tetralin content of less than 5% by weight .-%, based on the alkylbenzene.
  • alkylbenzenesulfonates whose alkylbenzenes have been prepared by the HF process, so that detergent tablets are preferred in which the alkylbenzenesulfonate compounds contain the alkali metal, preferably sodium, salts of C 8 -i 6 -, preferably C 9 3 alkybenzenesulfonic acids containing 2-phenyl isomer content below 22% by weight, based on the alkylbenzenesulfonic acid.
  • the detergent tablets according to the invention preferably contain the alkylbenzenesulfonate compounds in amounts of from 0.5 to 20% by weight, preferably from 1 to 15% by weight, particularly preferably from 2 to 10% by weight and in particular from 3 to 8 wt .-%, each based on the molded body weight.
  • the alkylbenzenesulfonate contents of 1 to 30% by weight, preferably 5 to 25% by weight and in particular 10 to 15% by weight, based in each case the molded body weight.
  • the total amount of alkylbenzenesulfonates can be introduced via ABS compounds, but it is also possible and within the scope of the present invention preferred that the washing and cleaning agent molded articles contain, in addition to the alkylbenzenesulfonate compounds, an alkylbenzenesulfonate-containing surfactant granulate.
  • the total amount of ABS is not introduced into the detergent tablets according to the invention via ABS compounds, but if other ways of incorporation - for example via an ABS-containing surfactant granulate - are selected, it is preferred that at least 20% by weight, preferably at least 30% by weight and in particular at least 40% by weight of the total alkyl benzene sulfonate contained in the molded bodies is introduced into the molded bodies via the alkyl benzene sulfonate compounds.
  • the amount introduced into the detergent tablets through the ABS compounds it is completely irrelevant whether these ABS compounds are only mixed when the individual components are mixed, i.e.
  • a surfactant granulate can be produced which, on the one hand, contains ABS compounds according to the invention, but on the other hand can also have a further ABS content which results, for example, from ABSS added during the granulation.
  • the washing and cleaning agent foils contain customary ingredients of washing and cleaning agents, in particular from the groups of surfactants and / or builders.
  • Further ingredients that can be used in the detergent tablets according to the invention are, for example, disintegration aids, bleaching agents, bleach activators, enzymes, dyes and fragrances, optical brighteners, polymers, foam inhibitors, etc.
  • the detergent tablets according to the invention can, in addition to the ABS, contain further surface-active substances from the group of anionic, nonionic, zwitterionic or cationic surfactants. hold, anionic surfactants are clearly preferred for economic reasons and because of their range of services.
  • Anionic surfactants used are, for example, those of the sulfonate and sulfate type.
  • Surfactants of the sulfonate type are, for example, olefin sulfonates, ie mixtures of alkene and hydroxyalkane sulfonates, and the disulfonates obtained, for example, from C 2 - ⁇ 8 -Monoolefmen with terminal or internal double bond by kidney sulphonated with gaseous sulfur trioxide and subsequent alkaline or acidic hydrolysis of the sulfonation products is considered.
  • alkanesulfonates which are for example obtained from C 2 - ⁇ 8 alkanes by sulfochlorination or sulfoxidation and subsequent hydrolysis or neutralization.
  • the esters of ⁇ -sulfofatty acids for example the ⁇ -sulfonated methyl esters of hydrogenated coconut, palm kernel or tallow fatty acids, are also suitable.
  • sulfonated fatty acid glycerol esters are sulfonated fatty acid glycerol esters.
  • Fatty acid glycerol esters are to be understood as meaning the mono-, di- and triesters and their mixtures as obtained in the production by esterification of a monoglycerol with 1 to 3 moles of fatty acid or in the transesterification of triglycerides with 0.3 to 2 moles of glycerol become.
  • Preferred sulfated fatty acid glycerol esters are the sulfate products of saturated fatty acids having 6 to 22 carbon atoms, for example caproic acid, caprylic acid, capric acid, myristic acid, lauric acid, palmitic acid, stearic acid or behenic acid.
  • alk (en) yl sulfates are the alkali and in particular the sodium salts of the sulfuric acid semiesters of the Ci 2 -C 8 fatty alcohols, for example from coconut oil alcohol, tallow fatty alcohol, lauryl, myristyl, cetyl or stearyl alcohol or the C 1 -C 20 oxo alcohols and those half-esters of secondary alcohols of this chain length are preferred.
  • alk (en) yl sulfates of the chain length mentioned which contain a synthetic, straight-chain alkyl radical prepared on a petrochemical basis and which have a degradation behavior analogous to that of the adequate compounds based on oleochemical raw materials.
  • C 2 -C 6 alkyl sulfates and C 12 - cis alkyl sulfates and C 4 -Ci 5 alkyl sulfates are preferred for washing technology reasons.
  • 2,3-alkyl sulfates which are produced, for example, according to US Pat. Nos. 3,234,258 or 5,075,041 and can be obtained as commercial products from Shell Oil Company under the name DAN ® are suitable anionic surfactants.
  • 21 alcohols such as 2-methyl-branched C 9 _n alcohols with an average of 3.5 moles of ethylene oxide (EO) or C 2 - ⁇ s fatty alcohols with 1 to 4 EO, are suitable. Because of their high foaming behavior, they are used in cleaning agents only in relatively small amounts, for example in amounts of 1 to 5% by weight.
  • Suitable anionic surfactants are also the salts of alkylsulfosuccinic acid, which are also referred to as sulfosuccinates or as sulfosuccinic acid esters and which are monoesters and / or diesters of sulfosuccinic acid with alcohols, preferably fatty alcohols and especially ethoxylated fatty alcohols.
  • Preferred sulfosuccinates contain C 8-0 8 fatty alcohol residues or mixtures thereof.
  • Particularly preferred sulfosuccinates contain a fatty alcohol residue which is derived from ethoxylated fatty alcohols, which in themselves are nonionic surfactants (description see below).
  • alk (en) ylsuccinic acid with preferably 8 to 18 carbon atoms in the alk (en) yl chain or salts thereof.
  • Soaps are particularly suitable as further anionic surfactants.
  • Saturated fatty acid soaps are suitable, such as the salts of lauric acid, myristic acid, palmitic acid, stearic acid, hydrogenated erucic acid and behenic acid, and in particular from natural fatty acids, e.g. Coconut, palm kernel or tallow fatty acids, derived soap mixtures.
  • the anionic surfactants can be in the form of their sodium, potassium or ammonium salts and also as soluble salts of organic bases, such as mono-, di- or triethanolamine.
  • the anionic surfactants are preferably in the form of their sodium or potassium salts, in particular in the form of the sodium salts.
  • detergent tablets are preferred which contain 5 to 50% by weight, preferably 7.5 to 40% by weight and in particular 10 to 20% by weight of anionic surfactant (s), based in each case on the Molded body weight, included.
  • anionic surfactants that are used in the detergent tablets according to the invention, there are no general conditions to be observed that prevent freedom of formulation.
  • preferred detergent tablets have a soap content which exceeds 0.2% by weight, based on the total weight of the tablet.
  • Anionic surfactants to be used with preference are the alkylbenzenesulfonates and fatty alcohol sulfates, with preferred detergent tablets 2 to 20% by weight, preferably 2.5 to 15% by weight and in particular 3 to 8% by weight of fatty alcohol sulfate (s) in each case based on the molded body weight
  • the nonionic surfactants used are preferably alkoxylated, advantageously ethoxylated, in particular primary alcohols having preferably 8 to 18 carbon atoms and an average of 1 to 12 moles of ethylene oxide (EO) per mole of alcohol in which the alcohol radical has a methyl or linear branching in the 2-position may be or may contain linear and methyl-branched radicals in the mixture, as are usually present in oxo alcohol radicals.
  • alcohol ethoxylates with linear residues of alcohols of native origin with 12 to 18 carbon atoms, for example from coconut, palm, tallow fat or oleyl alcohol, and an average of 2 to 8 EO per mole of alcohol are particularly preferred.
  • Preferred ethoxylated alcohols include, for example C12 - 14 - alcohols with 3 EO or 4 EO, C n-alcohol with 7 EO, C ⁇ 3 . ⁇ 5 alcohols containing 3 EO, 5 EO, 7 EO or 8 EO, C 12 - ⁇ 8 - alcohols with 3 EO, 5 EO or 7 EO and mixtures of these, such as mixtures of C 1 2.
  • the degrees of ethoxylation given represent statistical averages, which can be an integer or a fraction for a specific product.
  • Preferred alcohol ethoxylates have a narrow homolog distribution (narrow range ethoxylates, NRE).
  • fatty alcohols with more than 12 EO can also be used. Examples of this are tallow fatty alcohol with 14 EO, 25 EO, 30 EO or 40 EO.
  • Another class of preferably used nonionic surfactants which are used either as the sole nonionic surfactant or in combination with other nonionic surfactants, are alkoxylated, preferably ethoxylated or ethoxylated and propoxylated fatty acid alkyl esters, preferably with 1 to 4 carbon atoms in the alkyl chain, in particular Fatty acid methyl esters as described, for example, in Japanese patent application JP 58/217598 or which are preferably prepared by the process described in international patent application WO-A-90/13533.
  • alkyl polyglycosides Another class of nonionic surfactants that can be used advantageously are the alkyl polyglycosides (APG).
  • APG alkyl polyglycosides
  • Usable alkyl polyglycosides satisfy the general formula RO (G) z , in which R is a linear or branched, in particular methyl-branched, saturated or unsaturated, aliphatic radical having 8 to 22, preferably 12 to 18, carbon atoms and G is Is a symbol which stands for a glycose unit with 5 or 6 carbon atoms, preferably for glucose.
  • the degree of glycosidation z is between 1.0 and 4.0, preferably between 1.0 and 2.0 and in particular between 1.1 and 1.4.
  • Linear alkyl polyglucosides ie alkyl polyglycosides, in which the polyglycosyl radical is a glucose radical and the alkyl radical is an n-alkyl radical are preferably used.
  • the detergent tablets according to the invention can preferably contain alkyl polyglycosides, with APG contents in the tablet of more than 0.2% by weight, based on the total tablet, being preferred.
  • Particularly preferred detergent tablets contain APG in amounts of 0.2 to 10% by weight, preferably 0.2 to 5% by weight and in particular 0.5 to 3% by weight.
  • Nonionic surfactants of the amine oxide type for example N-coconut alkyl-N, N-dimethylamine oxide and N-tallow alkyl-N, N-dihydroxyethylamine oxide, and the fatty acid alkanolamides can also be suitable.
  • the amount of these nonionic surfactants is preferably not more than that of the ethoxylated fatty alcohols, in particular not more than half of them.
  • Other suitable surfactants are polyhydroxy fatty acid amides of the formula (II),
  • RCO stands for an aliphatic acyl radical with 6 to 22 carbon atoms
  • R for hydrogen, an alkyl or hydroxyalkyl radical with 1 to 4 carbon atoms
  • [Z] for a linear or branched polyhydroxyalkyl radical with 3 to 10 carbon atoms and 3 to 10 hydroxyl groups.
  • the polyhydroxy fatty acid amides are known substances which can usually be obtained by reductive amination of a reducing sugar with ammonia, an alkylamine or an alkanolamine and subsequent acylation with a fatty acid, a fatty acid alkyl ester or a fatty acid chloride.
  • the group of polyhydroxy fatty acid amides also includes compounds of the formula (III)
  • R represents a linear or branched alkyl or alkenyl radical having 7 to 12 carbon atoms
  • R 1 represents a linear, branched or cyclic alkyl radical or an aryl radical having 2 to 8 carbon atoms
  • R 2 represents a linear, branched or cyclic alkyl radical or an aryl radical or an oxy-alkyl radical having 1 to 8 carbon atoms
  • C 4 alkyl or phenyl radicals are preferred
  • [Z] stands for a linear polyhydroxyalkyl radical whose alkyl chain is substituted with at least two hydroxyl groups, or alkoxylated, preferably ethoxylated or propoxylated derivatives thereof Rest.
  • [Z] is preferably obtained by reductive amination of a reduced sugar, for example glucose, fructose, maltose. Lactose, galactose, mannose or xylose.
  • a reduced sugar for example glucose, fructose, maltose. Lactose, galactose, mannose or xylose.
  • the N-alkoxy- or N-aryloxy-substituted compounds can then, for example according to the teaching of international application WO-A-95/07331, be converted into the desired polyhydroxy fatty acid amides by reaction with fatty acid methyl esters in the presence of an alkoxide as catalyst.
  • builders are the most important ingredients in detergents and cleaning agents.
  • all builders commonly used in detergents and cleaning agents can be present, in particular thus zeolites, silicates, carbonates, organic cobuilders and - where there are no ecological prejudices against their use - also the phosphates.
  • Suitable crystalline, layered sodium silicates have the general formula NaMSi x 0 ⁇ + ⁇ 'H 2 O, where M is sodium or hydrogen, x is a number from 1.9 to 4 and y is a number from 0 to 20 and preferred values for x 2, 3 or 4.
  • M sodium or hydrogen
  • x is a number from 1.9 to 4
  • y is a number from 0 to 20 and preferred values for x 2, 3 or 4.
  • Such crystalline layered silicates are described, for example, in European patent application EP-A-0 164 514.
  • Preferred crystalline layered silicates of the formula given are those in which M represents sodium and x assumes the values 2 or 3.
  • both ⁇ - and ⁇ -sodium disilicate Na 2 Si 2 ⁇ 5 'yH 0 are preferred, with ⁇ -sodium disilicate being able to be obtained, for example, by the method described in international patent application WO-A-91/08171.
  • Amorphous sodium silicates with a module Na2 ⁇ : Si ⁇ 2 of 1: 2 to 1: 3.3, preferably from 1: 2 to 1: 2.8 and in particular from 1: 2 to 1: 2.6, which are delayed in dissolution, can also be used and have secondary washing properties.
  • the delay in dissolution compared to conventional amorphous sodium silicates can be caused in various ways, for example by surface treatment, compounding, compacting / compression or by overdrying.
  • the term “amo ⁇ h” is also understood to mean “roentgenamo ⁇ h”.
  • silicates at X-ray diffraction experiments do not provide sharp X-ray reflections, as are typical for crystalline substances, but at most one or more maxima of the scattered X-rays, which have a width of several degree units of the diffraction angle.
  • it can very well lead to particularly good builder properties if the silicate particles deliver washed-out or even sharp diffraction maxima in electron diffraction experiments.
  • This is to be integrated in such a way that the products have microcrystalline areas of size 10 to a few hundred nm, values up to max. 50 nm and in particular up to max. 20 nm are preferred.
  • Such so-called X-ray amorphous silicates which also have a delay in dissolution compared to conventional water glasses, are described, for example, in German patent application DE-A-44 00 024. Particularly preferred are compressed / compacted amorphous silicates, compounded amorphous silicates and over-dried X-ray silicates.
  • the finely crystalline, synthetic and bound water-containing zeolite used is preferably zeolite A and / or P.
  • zeolite P zeolite MAP® (commercial product from Crosfield) is particularly preferred.
  • zeolite X and mixtures of A, X and / or P are also suitable.
  • Commercially available and can preferably be used in the context of the present invention for example a co-crystallizate of zeolite X and zeolite A (about 80% by weight of zeolite X) ), which is sold by CONDEA Augusta SpA under the brand name VEGOBOND AX ® and by the formula
  • the zeolite can be used both as a builder in a granular compound and can also be used for a kind of "powdering" of the entire mixture to be used, usually both ways of incohering the zeolite into the premix.
  • Suitable zeolites have an average particle size of less than 10 ⁇ m (volume distribution; measurement method: Coulter Counter) and preferably contain 18 to 22% by weight, in particular 20 to 22% by weight, of bound water. It is of course also possible to use the generally known phosphates as builder substances, provided that such use should not be avoided for ecological reasons.
  • alkali metal phosphates with particular preference for pentasodium or pentapotassium triphosphate (sodium or potassium tripolyphosphate), have the greatest importance in the detergent and cleaning agent industry.
  • Alkali metal phosphates is the general term for the alkali metal (especially sodium and potassium) salts of the various phosphoric acids, in which one can distinguish between metaphosphoric acids (HP0) n and orthophosphoric acid H P0 4 in addition to higher molecular weight representatives.
  • the phosphates combine several advantages: They act as alkali carriers, prevent limescale deposits on machine parts and lime incrustations in tissues and also contribute to cleaning performance.
  • Sodium dihydrogen phosphate, NaH 2 P0 4 exists as a dihydrate (density 1.91 like “3 , melting point 60 °) and as a monohydrate (density 2.04 like “ 3 ). Both salts are white, water-soluble powders, which lose water of crystallization when heated and into the weakly acidic diphosphate (disodium hydrogen diphosphate, Na 2 H 2 P 2 0) at 200 ° C, and at higher temperature in sodium trimetaphosphate (Na 3 P 3 0) and Maddrell's salt (see below).
  • NaH 2 P0 4 is acidic; it occurs when phosphoric acid is adjusted to pH 4.5 with sodium hydroxide solution and the mash is sprayed.
  • Potassium dihydrogen phosphate (primary or monobasic potassium phosphate, potassium biphosphate, KDP), KH2PO 4 , is a white salt with a density of 2.33 gcm " , has a melting point of 253 ° [decomposition to form potassium polyphosphate (KP0) x ] and is easily soluble in Water.
  • Disodium hydrogen phosphate (secondary sodium phosphate), Na 2 HPO 4 , is a colorless, very easily water-soluble crystalline salt. It exists anhydrous and with 2 mol. (Density 2.066 gladly “3 , water loss at 95 °), 7 mol. (Density 1.68 gladly “ 3 , melting point 48 ° with loss of 5 H 2 0) and 12 mol. Water ( Density 1.52 "3 , melting point 35 ° with loss of 5 H 2 O), becomes anhydrous at 100 ° and changes to diphosphate Na 4 P 0 7 when heated more. Disodium hydrogenphosphate is used by neutralizing phosphoric acid with soda solution of phenolphthalein as an indicator posed. Dipotassium hydrogen phosphate (secondary or dibasic potassium phosphate), K 2 HP0, is an amorphous, white salt that is easily soluble in water.
  • Trisodium phosphate, tertiary sodium phosphate, Na P0 4 are colorless crystals that like a dodecahydrate a density of 1.62 "3 and a melting point of 73-76 ° C (decomposition), as a decahydrate (corresponding to 19-20% P2O 5 ) Melting point of 100 ° C and in anhydrous form (corresponding to 39-40% P2O5) a density of 2.536 like "3 .
  • Trisodium phosphate is readily soluble in water with an alkaline reaction and is produced by evaporating a solution of exactly 1 mol of disodium phosphate and 1 mol of NaOH.
  • Tripotassium phosphate (tertiary or three-base potassium phosphate), K 3 P0 4 , is a white, deliquescent, granular powder with a density of 2.56 "3 , has a melting point of 1340 ° and is readily soluble in water with an alkaline reaction Heating of Thomas slag with coal and potassium sulfate Despite the higher price, the more soluble, therefore highly effective, potassium phosphates are often preferred over corresponding sodium compounds in the cleaning agent industry.
  • Tetrasodium diphosphate (sodium pyrophosphate), Na 4 P 2 ⁇ 7, exists in anhydrous form (density 2.534 like “3 , melting point 988 °, also given 880 °) and as decahydrate (density 1.815-1.836 like " 3 , melting point 94 ° with loss of water). Substances are colorless crystals that are soluble in water with an alkaline reaction. Na P 2 0 7 is formed by heating disodium phosphate to> 200 ° or by reacting phosphoric acid with soda in a stoichiometric ratio and dewatering the solution by spraying. The decahydrate complexes heavy metal salts and hardness formers and therefore reduces the hardness of the water.
  • Potassium diphosphate (potassium pyrophosphate), K4P2O 7 , exists in the form of the trihydrate and is a colorless, hygroscopic powder with a density of 2.33 "3 , which is soluble in water, the pH of the 1% solution at 25 ° Is 10.4.
  • Sodium and potassium phosphates in which one can differentiate cyclic representatives, the sodium or potassium metaphosphates and chain-like types, the sodium or potassium polyphosphates. A large number of terms are used in particular for the latter: melt or glow phosphates, Graham's salt, Kurrol's and Maddrell's salt. All higher sodium and potassium phosphates are collectively referred to as condensed phosphates.
  • pentasodium triphosphate In the production of pentasodium triphosphate, phosphoric acid is reacted with sodium carbonate solution or sodium hydroxide solution in a stoichiometric ratio and the solution is dewatered by spraying. Similar to Graham's salt and sodium diphosphate, pentasodium triphosphate dissolves many insoluble metal compounds (including lime soaps, etc.). Pentapotassium triphosphate, K 5 P 3 O ⁇ o (potassium tripolyphosphate), is commercially available, for example, in the form of a 50% by weight solution (> 23% P 2 O 5 , 25% K 2 0). The potassium polyphosphates are widely used in the detergent and cleaning agent industry. There are also sodium potassium tripolyphosphates which can also be used in the context of the present invention. These occur, for example, when hydrolyzing sodium trimetaphosphate with KOH:
  • these can be used just like sodium tripolyphosphate, potassium tripolyphosphate or mixtures of these two; Mixtures of sodium tripolyphosphate and sodium potassium tripolyphosphate or mixtures of potassium tripolyphosphate and sodium potassium tripolyphosphate or mixtures of sodium tripolyphosphate and potassium tripolyphosphate and sodium potassium tripolyphosphate can also be used according to the invention.
  • Organic cobuilders which can be used in the detergent tablets according to the invention are, in particular, polycarboxylates / polycarboxylic acids, polymeric polycarboxylates, aspartic acid, polyacetals, dextrins, other organic cobuilders (see below) and phosphonates are used. These classes of substances are described below.
  • Usable organic builders are, for example, the polycarboxylic acids which can be used in the form of their sodium salts, polycarboxylic acids being understood to mean those carboxylic acids which carry more than one acid function.
  • these are citric acid, adipic acid, succinic acid, glutaric acid, malic acid, tartaric acid, maleic acid, fumaric acid, sugar acids, ammocarboxylic acids, nitrilotriacetic acid (NTA), as long as such use is not objectionable for ecological reasons, and mixtures of these.
  • Preferred salts are the salts of polycarboxylic acids such as citric acid, adipic acid, succinic acid, glutaric acid, tartaric acid, sugar acids and mixtures of these.
  • the acids themselves can also be used.
  • the acids typically also have the property of an acidifying component and thus also serve to set a lower and milder pH of detergents or cleaning agents.
  • Citric acid, succinic acid, glutaric acid, adipic acid, gluconic acid and any mixtures thereof can be mentioned in particular.
  • Polymeric polycarboxylates are also suitable as builders, for example the alkali metal salts of polyacrylic acid or polymethacrylic acid, for example those with a relative molecular weight of 500 to 70,000 g / mol.
  • the molecular weights given for polymeric polycarboxylates are weight-average molecular weights M w of the particular acid form, which were determined in principle by means of gel permeation chromatography (GPC), a UV detector being used.
  • the measurement was carried out against an external polyacrylic acid standard, which provides realistic molecular weight values due to its structural relationship with the investigated polymers. This information differs significantly from the molecular weight information for which polystyrene sulfonic acids are used as standard.
  • the molecular weights measured against polystyrene sulfonic acids are generally significantly higher than the molecular weights given in this document.
  • Suitable polymers are, in particular, polyacrylates, which preferably have a molecular weight of 2,000 to 20,000 g / mol. Because of their superior solubility, the short-chain polyacrylates which have molar masses from 2000 to 10000 g / mol, and particularly preferably from 3000 to 5000 g / mol, can in turn be preferred from this group.
  • copolymeric polycarboxylates in particular those of acrylic acid with methacrylic acid and of acrylic acid or methacrylic acid with maleic acid.
  • Copolymers of acrylic acid with maleic acid which contain 50 to 90% by weight of acrylic acid and 50 to 10% by weight of maleic acid have proven to be particularly suitable.
  • Their relative molecular weight, based on free acids, is generally 2,000 to 70,000 g / mol, preferably 20,000 to 50,000 g / mol and in particular 30,000 to 40,000 g / mol.
  • the (co) polymeric polycarboxylates can be used either as a powder or as an aqueous solution.
  • the content of (co) polymeric polycarboxylates in the agents is preferably 0.5 to 20% by weight, in particular 3 to 10% by weight.
  • the polymers can also contain allylsulfonic acids, such as, for example, allyloxybenzenesulfonic acid and methallylsulfonic acid, as monomers.
  • allylsulfonic acids such as, for example, allyloxybenzenesulfonic acid and methallylsulfonic acid, as monomers.
  • biodegradable polymers composed of more than two different monomer units, for example those which contain salts of acrylic acid and maleic acid as well as vinyl alcohol or vinyl alcohol derivatives as monomers or those which contain salts of acrylic acid and 2-alkylallylsulfonic acid and sugar derivatives as monomers .
  • copolymers are those which are described in German patent applications DE-A-43 03 320 and DE-A-44 17 734 and which preferably contain acrolein and acrylic acid / acrylic acid salts or acrolein and vinyl acetate as monomers.
  • polymeric aminodicarboxylic acids their salts or their precursor substances.
  • Polyas- Paraginic acids or their salts and derivatives of which it is disclosed in German patent application DE-A-195 40 086 that, in addition to cobuilder properties, they also have a bleach-stabilizing effect.
  • polyacetals which can be obtained by reacting dialdehydes with polyolcarboxylic acids which have 5 to 7 carbon atoms and at least 3 hydroxyl groups.
  • Preferred polyacetals are obtained from dialdehydes such as glyoxal, glutaraldehyde, terephthalaldehyde and their mixtures and from polyol carboxylic acids such as gluconic acid and / or glucoheptonic acid.
  • Suitable organic builder substances are dextrins, for example oligomers or polymers of carbohydrates, which can be obtained by partial hydrolysis of starches.
  • the hydrolysis can be carried out by customary, for example acid or enzyme-catalyzed, methods. They are preferably hydrolysis products with average molar masses in the range from 400 to 500,000 g / mol.
  • DE dextrose equivalent
  • oxidized derivatives of such dextrins are their reaction products with oxidizing agents which are capable of oxidizing at least one alcohol function of the saccharide ring to the carboxylic acid function.
  • oxidizing agents capable of oxidizing at least one alcohol function of the saccharide ring to the carboxylic acid function.
  • Such oxidized dextrins and processes for their preparation are known, for example, from European patent applications EP-A-0 232 202, EP-A-0 427349, EP-A-0 472 042 and EP-A-0 542 496 and international patent applications WO 92 / 18542, WO 93/08251, WO 93/16110, WO 94/28030, WO 95/07303, WO 95/12619 and WO 95/20608 are known.
  • Oxydisuccinates and other derivatives of disuccinates, preferably ethylenediaminisisuccinate, are further suitable cobuilders.
  • Ethylene diamine N, N'-disuccinate (EDDS) is preferably used in the form of its sodium or magnesium salts.
  • Glycerol disuccinates and glycerol trisuccinates are also preferred in this context. Suitable amounts are 3 to 15% by weight in formulations containing zeolite and / or silicate.
  • organic cobuilders are, for example, acetylated hydroxycarboxylic acids or their salts, which may optionally also be in lactone form and which contain at least 4 carbon atoms and at least one hydroxyl group and a maximum of two acid groups.
  • Such cobuilders are described, for example, in international patent application WO 95/20029.
  • phosphonates are, in particular, hydroxyalkane or aminoalkane phosphonates.
  • hydroxyalkane phosphonates l-hydroxyethane-l, l-diphosphonate (HEDP) is of particular importance as a cobuilder. It is preferably used as the sodium salt, the disodium salt reacting neutrally and the tetrasodium salt in an alkaline manner (pH 9).
  • Preferred aminoalkane phosphonates are ethylenediaminetetrarethylenephosphonate (EDTMP), diethylenetriaminepentamethylenephosphonate (DTPMP) and their higher homologs.
  • HEDP is preferably used as the builder from the class of the phosphonates.
  • the aminoalkanephosphonates also have a pronounced ability to bind heavy metals. Accordingly, it may be preferred, particularly if the agents also contain bleach, to use aminoalkanephosphonates, in particular DTPMP, or to use mixtures of the phosphonates mentioned.
  • the amount of builder is usually between 10 and 70% by weight, preferably between 15 and 60% by weight and in particular between 20 and 50% by weight. How- the amount of builders used is therefore dependent on the intended use, so that bleach tablets can have higher amounts of builders (for example between 20 and 70% by weight, preferably between 25 and 65% by weight and in particular between 30 and 55% by weight) ), for example detergent tablets (usually 10 to 50% by weight, preferably 12.5 to 45% by weight and in particular between 17.5 and 37.5% by weight).
  • detergent tablets These three requirements are extremely difficult to master with many substance mixtures, so that direct tableting is not often used, particularly in the manufacture of detergent tablets.
  • the usual way of producing detergent tablets is therefore based on powdery components (“primary particles”) which are agglomerated or granulated by suitable processes to form secondary particles with a larger particle diameter. These granules or mixtures of different granules are then mixed with individual powdery additives and fed to the tableting.
  • the present invention therefore also relates to a process for the production of detergent tablets, characterized by the steps a) production of alkylbenzenesulfonate compounds with alkylbenzenesulfonate contents above 40% by weight, based on the compound, b) mixing with other processing components to form a compressible premix, c) compressing to shaped bodies.
  • the alkylbenzenesulfonate compounds prepared in step a) have alkylbenzenesulfonate contents above 50% by weight, preferably above 60% by weight and in particular above 70% by weight, based on the compound .
  • the ABS compounds in step a) are produced using customary methods, the production by granulation, preferably fluidized bed granulation, being preferred.
  • the raw materials for the production of the ABS compounds can be both the ABS pastes and the free ABSS.
  • For neutralization for example, alkaline solids, onto which the ABSS is sprayed, or aqueous alkalis can be used. In the latter case, ABSS and alkali are sprayed onto moving solid beds made of carrier material.
  • acid and alkali with compressed air in a hollow chamber nozzle and at the same time to neutralize and atomize.
  • Preferred detergent tablets in the context of the present invention are obtained by squeezing a particulate premix comprising at least one surfactant-containing granulate and at least one subsequently admixed powdery component.
  • the granules containing surfactant can be produced by conventional industrial granulation processes such as compacting, extrusion, mixer granulation, pelletization or fluidized bed granulation. It is advantageous for the later detergent tablets if the premix to be ve ⁇ resses has a bulk density that comes close to the usual compact detergent.
  • step b) one or more surfactant granules are treated as processing components in the premix and the particulate Premix has a bulk density of at least 500 g / 1, preferably at least 600 g / 1 and in particular at least 700 g / 1.
  • the or at least one of the surfactant granules (e) contains alkylbenzenesulfonates.
  • the surfactant-containing granules also meet certain particle size criteria. Methods according to the invention are preferred in which the surfactant-containing granules have particle sizes between 100 and 2000 ⁇ m, preferably between 200 and 1800 ⁇ m, particularly preferably between 400 and 1600 ⁇ m and in particular between 600 and 1400 ⁇ m.
  • the surfactant granules preferably also contain carriers which particularly preferably come from the group of builders.
  • Particularly advantageous processes are characterized in that the surfactant-containing granules contain anionic and / or nonionic surfactants and builders and total surfactant contents of at least 10% by weight, preferably at least 20% by weight and in particular at least 25% by weight, having.
  • ABS compounds are mixed with the surfactant granules and other processing components, ie added to the premix, or whether they are already used completely in the preparation of the surfactant granules.
  • Preferred processes according to the invention are characterized in that the surfactant-containing granules were prepared with the addition of all or part of the alkylbenzenesulfonate compounds produced in step a) with alkylbenzenesulfonate contents above 40% by weight, based on the compound.
  • At least 20% by weight, preferably at least 30% by weight and in particular at least 40% by weight of the total of the alkylbenzenesulfonate contained in the moldings in the form of the alkylbenzenesulfonate compounds prepared in step a) is incorporated into the Shaped body is introduced.
  • surfactant granules which contain part of the ABS contained in them in the form of ABS compounds, while the other part of the ABS reaches the surfactant granules in a different form, for example by spraying on ABSS. If such surfactant granules are produced, it is no longer necessary to add further amounts of ABS compound when producing the premix.
  • the total amount of ABS in the surfactant granules can also come from ABS compounds or the surfactant granules can be completely free of ABS compounds.
  • the only thing essential to the invention is that the premix to be ve ⁇ ress and thus the washing and cleaning agent moldings contain ABS compound with ABS contents above 40% by weight, based on the compound.
  • the premix Before the particulate premix is pressed into detergent tablets, the premix can be "powdered” with finely divided surface treatment agents. This can be of advantage for the quality and physical properties of both the premix (storage, molding) as well as the finished detergent tablets. Finely divided powdering agents are well known in the art, mostly zeolites, silicates or other inorganic salts being used. However, the premix is preferably “powdered” with finely divided zeolite, zeolites of the faujasite type being preferred. In the context of the present invention, the term “faujasite-type zeolite” denotes all three zeolites which form the faujasite subgroup of the zeolite structure group 4 (compare Donald W.
  • zeolite Y and faujasite and mixtures of these compounds can also be used, the pure zeolite X being preferred.
  • Mixtures or cocrystallizates of zeolites of the faujasite type with other zeolites which do not necessarily have to belong to the zeolite structural group 4 can also be used as powdering agents, it being advantageous if at least 50% by weight of the powdering agent is used a zeolite of the faujasite type.
  • detergent tablets consist of a particulate premix which contains granular components and subsequently admixed powdery substances
  • the or one of the subsequently mixed powdered components is a zeolite of the faujasite type with particle sizes below 100 ⁇ m, preferably below 100 ⁇ m and in particular below 5 ⁇ m and is at least 0.2% by weight, preferably at least 0.5% by weight and in particular more than 1% by weight %> of the premix to be consumed.
  • the detergent tablets according to the invention can contain further ingredients from the group of bleaching agents, bleach activators, disintegration aids, enzymes, pH regulators which are customary in detergents and cleaning agents , Fragrances, perfume carriers, fluorescent agents, dyes, foam inhibitors, silicone oils, anti-redeposition agents, optical brighteners, graying inhibitors, color transfer inhibitors and corrosion inhibitors.
  • sodium perborate tetrahydrate and sodium perborate monohydrate are of particular importance.
  • Other usable bleaching agents are, for example, sodium percarbonate, peroxypyrophosphates, citrate perhydrates and H2O2-providing peracidic salts or peracids, such as perbenzoates, peroxophthalates, diperazelaic acid, phthaloiminoperacid or diperdodecanedioic acid. Even when using the bleaching agents, it is possible to dispense with the use of surfactants and / or builders, so that pure bleach tablets can be produced.
  • bleaching agents from the group of organic bleaching agents can also be used.
  • Typical organic bleaching agents are the diacyl peroxides, such as dibenzoyl peroxide.
  • Other typical organic bleaching agents are peroxy acids, examples of which include alkyl peroxy acids and aryl peroxy acids.
  • Preferred representatives are (a) peroxybenzoic acid and its ring-substituted derivatives, such as alkylperoxybenzoic acids, but also peroxy- ⁇ -naphthoic acid and magnesium monophthalate, (b) the aliphatic or substituted aliphatic peroxyacids, such as peroxylauric acid, peroxystearic acid, ⁇ -phthalimidopercapid [Phthaloiminoperoxyhexanoic acid (PAP)], o-carboxybenzamidoperoxycaproic acid, N-nonenylamidoperadipic acid and N-nonenylamidopersuccinate, and (c) aliphatic and araliphatic peroxydicarboxylic acids, such as 1,12-diperoxycarboxylic acid, 1,9-diperoxyazelaic acid, diperocyseboxyacid, diperoxyacid acid, diperoxyacid acid, diperoxy acid, Decyldiper
  • Chlorine or bromine-releasing substances can also be used as bleaching agents in molded articles for automatic dishwashing.
  • Suitable materials which release chlorine or bromine include, for example, heterocyclic N-bromo- and N-chloramides, for example trichloroisocyanuric acid, tribromoisocyanuric acid,
  • DICA dichloroisocyanuric acid
  • Hydantoin compounds such as 1,3-dichloro-5,5-dimethylhydanthoin are also suitable.
  • bleach activators can be incorporated into the detergent tablets according to the invention.
  • Bleach activators which can be used are compounds which, under perhydrolysis conditions, give aliphatic peroxocarboxylic acids having preferably 1 to 10 C atoms, in particular 2 to 4 C atoms, and / or optionally substituted perbenzoic acid.
  • Suitable substances are those which carry O- and / or N-acyl groups of the number of carbon atoms mentioned and / or optionally substituted benzoyl groups.
  • TAED te
  • bleach catalysts can also be incorporated into the moldings.
  • these fabrics fen are bleach-enhancing transition metal salts or transition metal complexes such as Mn, Fe, Co, Ru or Mo salt complexes or carbonyl complexes.
  • Mn, Fe, Co, Ru, Mo, Ti, V and Cu complexes with N-containing tripod ligands as well as Co, Fe, Cu and Ru amine complexes can also be used as bleaching catalysts.
  • tablet disintegrants In order to facilitate the disintegration of highly compressed moldings, it is possible to incorporate disintegration aids, so-called tablet disintegrants, in order to shorten the disintegration times.
  • tablet disintegrants or disintegration accelerators are understood as auxiliary substances which are suitable for the rapid Disintegration of tablets in water or gastric juice and release of the pharmaceuticals in an absorbable form.
  • Preferred detergent tablets contain 0.5 to 10% by weight, preferably 3 to 8% by weight and in particular 4 to 6% by weight of a disintegration aid, in each case based on the molded article weight.
  • Disintegration agents based on cellulose are used as preferred disintegration agents in the context of the present invention, so that preferred detergent tablets form such a disintegration agent based on cellulose in amounts of 0.5 to 10% by weight, preferably 3 to 8% by weight and in particular 4 up to 6% by weight contain.
  • Pure cellulose has the formal gross composition (C ⁇ HioOs, and formally considered a ß-1,4-polyacetal of cellobiose, which in turn is made up of two molecules of glucose.
  • Suitable celluloses consist of about 500 to 5000 glucose units and therefore have average molar masses of 50,000 to 500,000.
  • Cellulose-based disintegrants which can be used in the context of the present invention are also cellulose derivatives which can be obtained from cellulose by polymer-analogous reactions.
  • Such chemically modified celluloses include, for example, products from esterifications or etherifications in to which hydroxy hydrogen atoms have been substituted, but celluloses in which the hydroxyl groups have been replaced by functional groups which are not bonded via an oxygen atom can also be used as cellulose derivatives, for example alkali celluloses belong to the group of cellulose derivatives , Carboxymethylc ellulose (CMC), cellulose esters and ethers and aminocelluloses.
  • CMC Carboxymethylc ellulose
  • the cellulose derivatives mentioned are preferably not used alone as a cellulose-based disintegrant, but are used in a mixture with cellulose.
  • the content of cellulose derivatives in these mixtures is preferably below 50% by weight, particularly preferably below 20% by weight, based on the cellulose-based disintegrant. Pure cellulose which is free of cellulose derivatives is particularly preferably used as the cellulose-based disintegrant.
  • Microcrystalline cellulose can be used as a further cellulose-based disintegrant or as a component of this component.
  • This microcrystalline cellulose is obtained by partial hydrolysis of celluloses under conditions which only attack and completely dissolve the amorphous areas (approx. 30% of the total cellulose mass) of the celluloses, but leave the crystalline areas (approx. 70%) undamaged.
  • a subsequent disaggregation of the microfine celluloses resulting from the hydrolysis provides the microcrystalline celluloses, which have primary particle sizes of approximately 5 ⁇ m and can be compacted, for example, to granules with an average particle size of 200 ⁇ m.
  • Particularly suitable enzymes are those from the classes of hydrolases such as proteases, esterases, lipases or lipolytically active enzymes, amylases, cellulases or other glycosyl hydrolases and mixtures of the enzymes mentioned. All these hydrolases help to remove stains such as protein, fat or starchy stains and graying in the laundry. Cellulases and other glycosyl hydrolases can also help to retain color and increase the softness of the textile by removing pilling and microfibrils. Oxidoreductases can also be used for bleaching or for inhibiting color transfer.
  • hydrolases such as proteases, esterases, lipases or lipolytically active enzymes, amylases, cellulases or other glycosyl hydrolases and mixtures of the enzymes mentioned. All these hydrolases help to remove stains such as protein, fat or starchy stains and graying in the laundry. Cellulases and other glycosyl hydrolases can also help to retain color and increase
  • Bacillus subtilis Bacillus licheniformis
  • Streptomyceus griseus Streptomyceus griseus
  • Coprinus Cinereus and Humicola insolens as well as enzymatic active ingredients obtained from their genetically modified variants.
  • Proteases of the subtilisin type and in particular proteases which are obtained from Bacillus lentus are preferably used.
  • Enzyme mixtures for example, from protease and amylase or protease and lipase or lipolytically active enzymes or protease and cellulase or from cellulase and lipase or lipolytically active enzymes or from protease, amylase and lipase or lipolytically active enzymes or protease, lipase or lipolytically active enzymes and cellulase, but in particular protease and / or lipase-containing mixtures or mixtures with lipolytically active enzymes of particular interest.
  • Known cutinases are examples of such lipolytically active enzymes.
  • Peroxidases or oxidases have also proven to be suitable in some cases.
  • Suitable amylases include in particular alpha-amylases, iso-amylases, pullulanases and pectinases.
  • Cellobiohydrolases, endoglucanases and glucosidases, which are also called cellobiases, or mixtures thereof, are preferably used as cellulases. Since different cellulase types differ in their CMCase and avicelase activities, the desired activities can be set by targeted mixtures of the cellulases.
  • the enzymes can be adsorbed on carriers or embedded in coating substances to protect them against premature decomposition.
  • the proportion of the enzymes, enzyme mixtures or enzyme granules can be, for example, about 0.1 to 5% by weight, preferably 0.5 to about 4.5% by weight.
  • the detergent tablets can also contain components that positively influence the oil and fat washability from textiles (so-called soil repellents). This effect becomes particularly clear when a textile is soiled that has already been washed several times beforehand with a detergent according to the invention which contains this oil and fat-dissolving component.
  • the preferred oil and fat-dissolving components include, for example, nonionic cellulose ethers such as methyl cellulose and methyl hydroxypropyl cellulose with a proportion of methoxyl groups of 15 to 30% by weight and of hydroxypropoxyl groups of 1 to 15% by weight, in each case based on the nonionic cellulose ether, and the polymers of phthalic acid and / or terephthalic acid or their derivatives known from the prior art, in particular polymers of ethylene terephthalates and / or polyethylene glycol terephthalates or anionically and / or nonionically modified derivatives thereof. Of these, the sulfonated derivatives of phthalic acid and terephthalic acid polymers are particularly preferred.
  • the shaped bodies can contain derivatives of diaminostilbenedisulfonic acid or their alkali metal salts as optical brighteners. Suitable are e.g. Salts of 4,4'-bis (2-anilino-4-mo ⁇ holino-l, 3,5-triazinyl-6-amino) stilbene-2,2'-disulfonic acid or compounds of the same structure which, instead of the Mo ⁇ holino group, have a diethanolamino group , a methylamino group, an anilino group or a 2-methoxyethylamino group.
  • brighteners of the substituted diphenylstyryl type may be present, e.g.
  • Dyes and fragrances are added to the detergent tablets according to the invention in order to improve the aesthetic impression of the products and to provide the consumer with a visually and sensorially "typical and unmistakable" product.
  • Individual fragrance compounds for example the synthetic products of the ester, ether, aldehyde, ketone, alcohol and hydrocarbon type, can be used as perfume oils or fragrances.
  • Fragrance compounds of the ester type are, for example, benzyl acetate, phenoxyethyl isobutyrate, p-tert.- Butylcyclohexyl acetate, lmalyl acetate, dimethylbenzyl carbinyl acetate, phenylethyl acetate, linalyl benzoate, benzyl formate, ethyl methylphenyl glycinate, allylcyclohexyl propionate, styrallyl propionate and benzyl salicylate.
  • the ethers include, for example, benzylethyl ether, the aldehydes, for example, the linear alkanals with 8-18 C atoms, citral, citronellal, citronellyloxyacetaldehyde, cyclamenaldehyde, hydroxycitronellal, lilial and bourgeonal, the ketones, for example, the jonones, oc -Isomethylionon and methyl-cedrylketone, the alcohols anethole, citronellol, eugenol, geraniol, linalool, phenylethyl alcohol and terpineol, the hydrocarbons mainly include tephenols such as limonene and pinene.
  • perfume oils can also contain natural fragrance mixtures such as are obtainable from plant sources, for example pine, citrus, jasmine, patchouly, rose or ylang-ylang oil. Also suitable are muscatel, sage oil, chamomile oil, clove oil, lemon balm oil, mint oil, cinnamon leaf oil, linden blossom oil, juniper berry oil, vetiver oil, olibanum oil, galbanum oil and labdanum oil as well as orange blossom oil, neroliol, orange peel oil and sandalwood oil.
  • the dye content of the agents according to the invention is usually less than 0.01% by weight, while fragrances can make up up to 2% by weight of the total formulation.
  • the fragrances can be incorporated directly into the agents according to the invention, but it can also be advantageous to apply the fragrances to carriers which increase the adhesion of the perfume to the laundry and ensure a long-lasting fragrance of the textiles due to a slower fragrance release.
  • Cyclodextrins for example, have proven useful as such carrier materials, and the cyclodextrin-perfume complexes can additionally be coated with further auxiliaries.
  • the agents according to the invention can be colored with suitable dyes.
  • Preferred dyes the selection of which is not difficult for the person skilled in the art, have a high storage stability and insensitivity to the other ingredients of the compositions and to light, and no pronounced substantivity to textile fibers, in order not to dye them.
  • the molded articles according to the invention are first produced by dry mixing the constituents, which can be wholly or partially pregranulated, and then providing information, in particular feeding them into tablets, whereby conventional methods can be used.
  • the premix is compacted in a so-called die between two punches to form a solid compact. This process, which is briefly referred to below as tabletting, is divided into four sections: metering, compression (elastic deformation), plastic deformation and ejection.
  • the premix is introduced into the die, the filling quantity and thus the weight and the shape of the molded body being formed being determined by the position of the lower punch and the shape of the pressing tool.
  • the constant dosing, even at high mold throughputs, is preferably achieved by volumetric dosing of the premix.
  • the upper punch touches the premix and lowers further towards the lower punch. With this compression, the particles of the premix are pressed closer together, the cavity volume within the filling between the punches continuously decreasing. From a certain position of the upper punch (and thus from a certain pressure on the premix), the plastic deformation begins, in which the particles flow together and the molded body is formed.
  • the premix particles are also crushed and sintering of the premix occurs at even higher pressures.
  • the phase of elastic deformation is shortened further and further, so that the resulting shaped bodies can have more or less large cavities.
  • the finished molded article is pressed out of the die by the lower punch and transported away by subsequent transport devices.
  • the weight of the molded body is finally determined, since the compacts can still change their shape and size due to physical processes (stretching, crystallographic effects, cooling, etc.). Tableting takes place in commercially available tablet presses, which can in principle be equipped with single or double punches.
  • eccentric tablet presses are preferably used, in which the punch or stamps are fastened to an eccentric disc, which in turn is mounted on an axis with a certain rotational speed.
  • the movement of these rams is comparable to that of a conventional four-stroke engine.
  • the pressing can take place with one upper and one lower punch, but several punches can also be attached to one eccentric disk, the number of die holes being increased accordingly.
  • the throughputs of eccentric presses vary depending on the type from a few hundred to a maximum of 3000 tablets per hour.
  • rotary tablet presses are selected in which a larger number of dies is arranged in a circle on a so-called die table.
  • the number of matrices varies between 6 and 55 depending on the model, although larger matrices are also commercially available.
  • Each die on the die table is assigned an upper and lower punch, whereby the pressure can only be built up actively by the upper or lower punch, but also by both punches.
  • the die table and the stamps move about a common vertical axis, the stamps being brought into the positions for filling, compaction, plastic deformation and ejection by means of rail-like cam tracks during the rotation.
  • these cam tracks are supported by additional low-pressure pieces, low-pressure rails and lifting tracks.
  • the die is filled via a rigidly arranged feed device, the so-called filling shoe, which is connected to a storage container for the premix.
  • the pressing pressure on the premix can be individually adjusted via the pressing paths for the upper and lower punches, the pressure being built up by rolling the punch shaft heads past adjustable pressure rollers.
  • Rotary presses can also be provided with two filling shoes to increase the throughput, with only a semicircle having to be run through to produce a tablet.
  • All non-stick coatings known from the art are suitable for reducing stamp caking.
  • Plastic coatings, plastic inserts or plastic stamps are particularly advantageous.
  • Rotating punches have also proven to be advantageous, with the upper and lower punches being designed to be rotatable if possible.
  • a plastic insert can generally be dispensed with.
  • the stamp surfaces should be electropolished here. It was also shown that long pressing times are advantageous. These can be set with pressure rails, several pressure rollers or low rotor speeds. Since the fluctuations in the hardness of the tablet are caused by the fluctuations in the pressing forces, systems should be used which limit the pressing force.
  • elastic stamps, pneumatic compensators or resilient elements can be used in the force path.
  • the pressure roller can also be designed to be resilient.
  • Tableting machines suitable within the scope of the present invention are available, for example, from the companies Apparatebau Holzwarth GbR, Asperg, Wilhelm Fette GmbH, Schwarzenbek, Hofer GmbH, Weil, Hom & Noack Pharmatechnik GmbH, Worms, IMA Ve ⁇ ackungssysteme GmbH Viersen, KILIAN, Cologne, KOMAGE, Kell am See, KORSCH Pressen AG, Berlin, and Romaco GmbH, Worms.
  • Other providers include Dr. Herbert Pete, Vienna (AU), Mapag Maschinenbau AG, Bern (CH), BWI Manesty, Liveeool (GB), I. Holand Ltd., Nottingham (GB), Courtoy NV, Halle (BE / LU) and Me- diopharm Kamnik (SI).
  • the hydraulic double pressure press HPF 630 from LAEIS, D. Tablettierwerkmaschinee are for example from the companies Adams Tablettierwerkmaschinee, Dresden, Wilhelm Fett GmbH, Schwarzenbek, Klaus Hammer, Solingen, Herber% Söhne GmbH, Hamburg, Hofer GmbH, Weil, Hom & Noack, Pharmatechnik GmbH, Worms, Ritter Pharamatechnik GmbH, Hamburg, Romaco, GmbH, Worms and Notter negligencebau, Tamm available.
  • Other providers are e.g. Senss AG, Reinach (CH) and Medicopharm, Kamnik (SI).
  • the molded body can be manufactured in a predetermined spatial shape and a predetermined size. Practically all practical configurations can be considered as the spatial shape, for example, the design as a board, the bar or bar shape, cubes, cuboids and corresponding spatial elements with flat side surfaces, and in particular cylindrical configurations with a circular or oval cross section.
  • This last embodiment covers the presentation form from the tablet to compact cylinder pieces with a ratio of height to diameter above 1.
  • the portioned compacts can each be designed as separate individual elements that correspond to the predetermined dosage of detergents or cleaning agents. It is also possible, however, to form compacts which connect a plurality of such mass units in one compact, the portioned smaller units being easy to separate, in particular by predetermined predetermined breaking points.
  • the portioned compacts as tablets, in cylinder or cuboid form can be expedient, with a diameter / height ratio in the range from about 0.5: 2 to 2: 0.5 is preferred.
  • Commercial hydraulic presses, eccentric presses or rotary presses are suitable devices, in particular for the production of such pressed articles.
  • the spatial shape of another embodiment of the molded body is adapted in its dimensions to the induction chamber of commercially available household washing machines, so that the molded body can be dosed directly into the induction chamber without metering aid, where it dissolves during the induction process.
  • metering aid a metering aid
  • Another preferred molded body that can be produced has a plate-like or sheet-like structure with alternately thick long and thin short segments, so that individual segments of this "bolt" at the predetermined breaking points, which represent the short thin segments, are broken off and into the Machine can be entered.
  • This principle of the "bar-shaped" shaped body detergent can also be realized in other geometric shapes, for example vertically standing triangles, which are connected to one another only on one of their sides along the side.
  • the various components are not pressed into a uniform tablet, but that shaped bodies are obtained which have several layers, that is to say at least two layers. It is also possible that these different layers have different dissolving speeds. This can result in advantageous application properties of the molded body. If both for example, components are contained in the moldings that mutually influence each other negatively, so it is possible to integrate one component in the more rapidly soluble layer and to incorporate the other component in a more slowly soluble layer, so that the first component has already reacted if the second goes into solution.
  • the layer structure of the molded body can take place in a stack-like manner, with the inner layer (s) already loosening at the edges of the molded body when the outer layers have not yet been completely removed, but it is also possible for the inner layer (s) to be completely encased ) can be achieved by the layer (s) lying further outwards, which prevents the premature dissolving of components of the inner layer (s).
  • a molded body consists of at least three layers, i.e. two outer and at least one inner layer, at least one peroxy bleaching agent being contained in one of the inner layers, while in the case of the stacked molded body the two outer layers and in the shell-shaped molded body the outermost layers, however, are free of peroxy bleach. Furthermore, it is also possible to spatially separate peroxy bleaching agents and any bleach activators and / or enzymes that may be present in a molded body.
  • Such multilayer molded bodies have the advantage that they can be used not only via a dispensing chamber or via a metering device which is added to the washing liquor; rather, in such cases it is also possible to put the molded body into direct contact with the textiles in the machine without the risk of bleaching from bleaching agents and the like.
  • the bodies to be coated can, for example, be sprayed with aqueous solutions or emulsions, or else they can be coated using the melt coating method.
  • colored particles can also be incorporated into the molded body as optical differentiation respectively.
  • a white molded body can be colored homogeneously with colored, for example blue, red, green, yellow, etc., speckles.
  • the amount of colored speckles and their particle size should be adapted to the rest of the premix which forms the shaped body matrix from which the speckles emerge optically.
  • a tableting mixture has a particle size of 200 to 1800 ⁇ m
  • speckles that move in the same or coarser particle size will only achieve a homogeneous distribution above a threshold value of> 6% by weight, based on the tablet composition. Smaller quantities then lead to an optically unattractive accumulation of speckles in some shaped body areas, while other areas remain almost unspotted.
  • a homogeneous distribution of the speckles is already achieved with 2 to 3% by weight> color speckle particles if these particle sizes have between 200 and 800 ⁇ m.
  • a homogeneous speckling which can be achieved in the manner described above by adapting the speckle particle size and quantity to the premix, also makes it possible to visualize a layer structure of the shaped bodies.
  • two- or multi-layer molded bodies can be produced, one layer of which is undyed, while a second layer is highlighted by sprinkles.
  • This concept can also be applied, for example, to three-layer tablets in which one layer is undyed, the second is speckled and the third is colored through.
  • ring-core tablets or point tablets can also be colored or sprinkled, for example. The person skilled in the art has hardly any limits when varying these implementation options for optical differentiation.
  • the impact strength of cylindrical shaped bodies can be determined via the measured variable of the diametrical fracture stress. This can be determined according to 2P ⁇ Dt
  • ⁇ stands for diametrical fracture stress (DFS) in Pa
  • P is the force in N, which leads to the pressure exerted on the molded body, which causes the Bmch of the molded body
  • D is the molded body diameter in meters and t the height of the molded body.
  • Another object of the present invention is the use of alkylbenzenesulfonate compounds with alkylbenzenesulfonate contents above 40% by weight, based on the compound, to improve the hardness and the rate of disintegration of detergent tablets.
  • the physical properties of the moldings can be improved, as the following examples show:
  • a polymer compound was produced by spray drying and served as the basis for a granulate containing tenside.
  • sodium C 9 was . ⁇ 3 by spray neutralization of 97% - 50% alkyl benzene sulfonic acid with> NaOH in a fluidized bed a 75%> prepared sodium ABS compound.
  • the compositions of the two compounds are shown in Table 1.
  • the spray-dried polymer compound was granulated with other components (zeolite, fatty alcohol sulfate, NaOH, alkylbenzenesulfonic acid, nonionic surfactant, soda, silicate) in a 50 liter ploughshare mixer from Lödige.
  • the amounts of the substances used and the order of addition to the mixer are given in Table 2.
  • example E2 only part of the total of the alkylbenzenesulfonate in the form of the alkylbenzenesulfonic acid contained in the moldings was added during the granulation, the rest of the total amount of alkylbenzenesulfonate was added in the form of the ABS compound; However, compound added to the granulation batch.
  • composition of the spray-dried or spray-neutralized compounds [% by weight>]
  • the granules were in a fluidized bed apparatus from Glatt at a supply air temperature of 60 ° C. over a period of 30 minutes to a water content of 8.0 ⁇ 0.2% by weight. dried. After drying, fine particles ⁇ 0.6 mm and coarse particles> 1.6 mm were screened off. To determine the water content of the granules, 2 g of the granules were heated for 10 minutes at 130 ° C. on a type MA 30 device from Sartorius and the drying loss was determined gravimetrically.
  • the surfactant granules E1 and E2 or V were then processed with further components to form a compressible premix, after which the Ve ⁇ res- in a Korsch eccentric press solution to tablets (diameter: 44 mm, height: 22 mm, weight: 37.5 g).
  • the pressure was set so that two series of molded bodies were obtained (El, E2 and V or El ', E2' and V), which differ in their hardness.
  • Table 3 shows the composition of the premixes to be fed (and thus the shaped body).
  • the hardness of the tablets was measured after two days of storage by deforming the tablet to the surface, the force acting on the side surfaces of the tablet and the maximum force which the tablet withstood being determined.
  • Table 4 shows that the disintegration times of detergent tablets are significantly reduced by the use of the ABS compounds according to the invention, it being irrelevant whether the ABS compounds are added to the compressible premix or are added during the manufacture of the surfactant granules.

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Abstract

L'invention concerne des corps moulés de lavage et de nettoyage aux propriétés intéressantes et améliorées en termes d'application technique. Ces corps moulés de lavage et de nettoyage contiennent des composés d'alkyle benzène sulfonate (ABS) ayant une teneur en alkyle benzène sulfonate supérieure à 40 % en poids par rapport au composé.
PCT/EP1999/006412 1998-09-10 1999-09-01 Corps moules de lavage et de nettoyage contenant de l'alkyle benzene sulfonate WO2000015753A1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE1998141362 DE19841362A1 (de) 1998-09-10 1998-09-10 ABS-haltige Wasch- und Reinigungsmittelformkörper
DE19841362.9 1998-09-10

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WO2000015753A1 true WO2000015753A1 (fr) 2000-03-23

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Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE19903290A1 (de) * 1999-01-28 2000-08-03 Henkel Kgaa Wasch- und Reinigungsmittelformkörper mit definiertem Aniontensidverhalten

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1004596A (en) * 1962-03-07 1965-09-15 Procter & Gamble Detergent tablet
EP0014979A1 (fr) * 1979-02-23 1980-09-03 Henkel Kommanditgesellschaft auf Aktien Procédé de fabrication de blocs de rinçage pour l'hygiène des toilettes
GB2205580A (en) * 1987-06-04 1988-12-14 Procter & Gamble Detergent bars
EP0481793A1 (fr) * 1990-10-19 1992-04-22 Unilever Plc Compositions détergentes sous forme de tablettes
EP0522766A2 (fr) * 1991-07-01 1993-01-13 Unilever Plc Compositions détergentes sous forme de tablettes
US5449473A (en) * 1991-07-03 1995-09-12 Kiwi Brands Inc. Lavatory cleansing and sanitizing blocks containing a halogen release bleach and a polybutene stabilizer

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1004596A (en) * 1962-03-07 1965-09-15 Procter & Gamble Detergent tablet
EP0014979A1 (fr) * 1979-02-23 1980-09-03 Henkel Kommanditgesellschaft auf Aktien Procédé de fabrication de blocs de rinçage pour l'hygiène des toilettes
GB2205580A (en) * 1987-06-04 1988-12-14 Procter & Gamble Detergent bars
EP0481793A1 (fr) * 1990-10-19 1992-04-22 Unilever Plc Compositions détergentes sous forme de tablettes
EP0522766A2 (fr) * 1991-07-01 1993-01-13 Unilever Plc Compositions détergentes sous forme de tablettes
US5449473A (en) * 1991-07-03 1995-09-12 Kiwi Brands Inc. Lavatory cleansing and sanitizing blocks containing a halogen release bleach and a polybutene stabilizer

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