EP0340589A1 - Detergents in the form of fusible shaped bodies - Google Patents
Detergents in the form of fusible shaped bodies Download PDFInfo
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- EP0340589A1 EP0340589A1 EP89107370A EP89107370A EP0340589A1 EP 0340589 A1 EP0340589 A1 EP 0340589A1 EP 89107370 A EP89107370 A EP 89107370A EP 89107370 A EP89107370 A EP 89107370A EP 0340589 A1 EP0340589 A1 EP 0340589A1
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Classifications
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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
- C11D3/00—Other compounding ingredients of detergent compositions covered in group C11D1/00
- C11D3/16—Organic compounds
- C11D3/37—Polymers
- C11D3/3703—Macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
- C11D3/3707—Polyethers, e.g. polyalkyleneoxides
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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
- C11D17/0052—Cast detergent compositions
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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
- C11D3/00—Other compounding ingredients of detergent compositions covered in group C11D1/00
- C11D3/02—Inorganic compounds ; Elemental compounds
- C11D3/04—Water-soluble compounds
- C11D3/08—Silicates
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- D—TEXTILES; PAPER
- D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
- D06F—LAUNDERING, DRYING, IRONING, PRESSING OR FOLDING TEXTILE ARTICLES
- D06F39/00—Details of washing machines not specific to a single type of machines covered by groups D06F9/00 - D06F27/00
- D06F39/02—Devices for adding soap or other washing agents
Definitions
- the invention relates to a detergent which is intended in particular for use in commercial laundries. These laundries usually use softened water, which is why the detergent content of builder salts that bind the hardness of lime is comparatively low compared to a household detergent, while the content of strongly alkaline builder salts, in particular metasilicates, is usually much higher. Due to the high level of alkalinity, powdery agents require special precautions when handling them and because they tend to clump together when exposed to moisture. Although it is known that such agents can also be stored and metered as liquid concentrates, so-called stock lyes, the technical systems required for this are not suitable for every location because of their increased expenditure and space requirements.
- the tablet, piece or block form is a suitable form.
- the agents be dissolved quickly and completely in the washing-up device of the washing machines in order to enable short work cycles.
- pieces of this type must be sufficiently stable against mechanical stress and so compact that layer-by-layer, uniform dissolution without disintegration of the shaped body enables them becomes. Crumbling powder compacts often cause hard deposits in the induction boxes.
- the preferred amount is 40 to 60% by weight and in particular 45 to 55% by weight.
- Component (B) consists of at least one polyanionic builder salt from the class of the polyphosphates, nitrilotriacetic acid, zeolite, polyphosphonic acids and (co) polymeric carboxylic acids in the form of the sodium salts.
- Their total amount is 4 to 25% by weight, preferably 5 to 20% by weight and in particular 7 to 15% by weight.
- polyphosphate sodium tripolyphosphate (TPP), which can be present in proportions of 0 to 10% by weight, preferably 0 to 5% by weight.
- TPP sodium tripolyphosphate
- component (B) advantageously consists of nitrilotriacetate (NTA) or zeolite or NTA-zeolite mixtures or of zeolite in a mixture with (co) polymeric carboxylic acids which act as so-called co-builders and threshold active ingredients.
- NTA nitrilotriacetate
- zeolite zeolite or NTA-zeolite mixtures or of zeolite in a mixture with (co) polymeric carboxylic acids which act as so-called co-builders and threshold active ingredients.
- polyphosphonates also have these properties.
- NTA as a phosphate substitute can be used in amounts of 0 to 7, preferably 0 to 6 and in particular 0 to 5% by weight. These amounts refer to anhydrous trisodium salt.
- Preferred phosphate substitutes are finely crystalline, synthetic, water-containing zeolites of the NaA type, which have a calcium binding capacity in the range from 100 to 200 mg CaO / g (according to the information in DE 22 24 837). Their particle size is usually in the range from 1 to 10 ⁇ m. The content of these zeolites is 0 to 15, preferably 0 to 10% by weight. Agents without phosphate or without NTA advantageously contain 5 to 10% by weight of zeolite.
- the zeolite is preferably used together with polyanionic co-builders. These include compounds from the class of polyphosphonic acids and homo- or copolymeric polycarboxylic acids, derived from acrylic acid, methacrylic acid, maleic acid and olefinic unsaturated, copolymerizable compounds.
- Suitable phosphonic acids or phosphonic acid salts 1-hydroxyethane-1,1-diphosphonate, ethylenediamine tetramethylene phosphonate (EDTMP) and diethylenetriamine pentamethylene phosphonate, mostly in the form of their sodium salts and their mixtures.
- the amounts are usually up to 2.0% by weight, based on the composition, preferably 0.2 to 1% by weight, based on the sodium salt. In the case of the diphosphonate, this amount refers to the tri sodium salt, in the case of tetraphosphonate on the hexasodium salt.
- co-builders are homopolymers of acrylic acid and methacrylic acid, copolymers of acrylic acid with methacrylic acid and copolymers of acrylic acid, methacrylic acid or maleic acid with vinyl ethers, such as vinyl methyl ether or vinyl ethyl ether, furthermore with vinyl esters, such as vinyl acetate or vinyl propionate, acrylamide, methacrylamide and with ethylene, Propylene or styrene.
- vinyl ethers such as vinyl methyl ether or vinyl ethyl ether
- vinyl esters such as vinyl acetate or vinyl propionate
- acrylamide, methacrylamide and with ethylene, Propylene or styrene are particularly useful co-builders.
- the proportion thereof in the interest of sufficient water solubility is not more than 70 mole percent, preferably less than 60 mole percent.
- Copolymers of acrylic acid or methacrylic acid with maleic acid as are characterized, for example, in EP 25 551-B 1, have proven to be particularly suitable. These are copolymers which contain 40 to 90 percent by weight of acrylic acid. Copolymers in which 50 to 85% by weight of acrylic acid and 50 to 15% by weight of maleic acid are present are particularly preferred.
- the (co) polymeric carboxylic acids mentioned can also be used without the use of zeolites.
- their proportion can be up to 7% by weight, preferably up to 6% by weight, based on neutral reacting, i.e. H. in aqueous solution having a pH of 7 to 8 sodium salt.
- their proportion can be reduced, for example to proportions up to 6%, preferably 0.5 to 5% by weight and in particular 1 to 4% by weight.
- nonionic surfactants additive products of 2 to 20, preferably 3 to 15 moles of ethylene oxide (EO) with 1 mole of a compound having essentially 10 to 20 carbon atoms from the group of the alcohols can be used as nonionic surfactants (component C).
- Suitable nonionic surfactants are derived from primary alcohols, e.g. on coconut or tallow fatty alcohols, oleyl alcohol, oxo alcohols, or on secondary alcohols with 8 to 18, preferably 12 to 18 carbon atoms.
- Combinations of water-soluble nonionic surfactants (component C1) and water-insoluble or water-dispersible nonionic surfactants (component C2) are preferably used.
- Component C1 includes those with 6 to 15 EO and an HLB value of more than 11, component C2 includes those with 2 to 6 EO and an HLB value of 11 or less.
- the ratio of C1 to C2 can be 2: 1 to 1: 4, preferably 1: 1 to 1: 3.
- the nonionic surfactants can also have propylene glycol ether groups (PO). These can be arranged at the end or distributed statistically with the EO groups.
- Preferred compounds of this class are those of the type R- (PO) x - (EO) y , in which R is the hydrophobic radical, x are numbers from 0.5 to 3 and y numbers from 3 to 20.
- nonionic surfactants are ethoxylates of alkylphenols, 1,2-diols, fatty acids and fatty acid amides and block polymers of polypropylene glycol and polyethylene glycol or alkoxylated alkylenediamines (Pluronics and Tetronics type). Furthermore, the above-described nonionic surfactants of the EO type can be partially replaced by alkyl polyglycosides. Suitable alkyl polyglycosides have, for example, a C8 ⁇ 16 alkyl radical and an oligomeric glycoside radical with 1.5 to 6 glucose groups. Alkyl glycoside-type surfactants are preferably combined with nonionic ethoxylate surfactants, for example in a ratio of 5: 1 to 1: 5.
- the content of the agents in nonionic surfactants or nonionic surfactant mixtures is 10 to 30% by weight, preferably 15 to 25% by weight and in particular 18 to 22% by weight.
- the agents can optionally also contain anionic surfactants, which are referred to as component E.
- anionic surfactants which are referred to as component E.
- Soaps and surfactants of the sulfonate or sulfate type are suitable. Contents of up to 5% by weight, in some cases up to 10% by weight, of anionic surfactants increase the washing performance, but usually lead to an undesirable foam activity. This foam activity can be reduced by adding suitable foam inhibitors.
- Organopolysilixanes in particular polydimethylsiloxanes and mixtures thereof with silica or silanized silica, hydrocarbon oils and waxes, microcrystalline waxes and bis-acylalkylenediamines derived from C2 tilllalkylenediamines with long-chain acyl residues containing 14 to 22 carbon atoms (fatty acid residues) are suitable .
- Mixtures of such foam inhibitors are also advantageously used.
- the amount of such foam inhibitors in the compositions depends on the amount and the foam activity of the synthetic anionic surfactants and is up to 5% by weight, preferably 0.5 to 3% by weight, based on the anionic surfactant.
- Suitable soaps are derived from natural or synthetic, saturated or monounsaturated fatty acids with 12 to 22 carbon atoms. Are particularly suitable from natural fatty acids such. B. coconut, palm kernel or tallow fatty acid derived soap mixtures. Preferred are those which are composed of 50 to 100% of saturated C12 ⁇ 18 fatty acid soaps and 0 to 50% of oleic acid soap. Their proportion can be up to 10% by weight, preferably up to 4% by weight, based on sodium soaps.
- Usable surfactants of the sulfonate type are linear alkylbenzenesulfonates (C9 ⁇ 13-alkyl) and olefin sulfonates, ie mixtures of alkene and hydroxylalkanesulfonates as well as disulfonates, as can be obtained, for example, from C12 ⁇ 1inen monoolefins with a terminal or internal double bond by sulfonating with gaseous sulfur trioxide and subsequent receives alkaline hydrolysis of the sulfonation products.
- Alkanesulfonates made from C12 ⁇ 18 alkanes by sulfochlorination or sulfo-oxidation and subsequent hydrolysis or neutralization are available, and alphasulfonated hydrogenated coconut, palm kernel or tallow fatty acids and their methyl or ethyl esters and mixtures thereof.
- surfactants containing sulfonate groups preference is given to the alkylbenzenesulfonates, alpha-sulfofatty acid ester salts and the alpha-sulfofatty acid ester disalts. They are in the form of their sodium salts. Their proportion can be up to 5% by weight, in some cases up to 8% by weight. It is preferably at most 2% by weight.
- the binders (component D) contain 2 to 15% by weight, preferably 2 to 10% by weight and in particular 3 to 8% by weight, of water-soluble, wax-like compounds from the class of polyethylene glycols with a molecular weight of at least 1100 and their alkyl ethers.
- the molecular weight of the polyglycol ether is preferably from 1300 to 40,000 and, if it has no alkyl groups, in particular from 1500 to 20,000.
- the alkyl chain can have 6 to 24 C atoms, preferably 10 to 18 C atoms.
- Alkyl polyglycol ethers derived from C14 ⁇ 18 alcohols or alcohol mixtures (for example tallow alcohol) which have 25 to 100, preferably 30 to 50, ethylene glycol ether groups have proven particularly suitable. Unsubstituted and alkyl-substituted polyethers can also be present in a mixture.
- the agents can also contain compounds containing active oxygen, such as sodium perborate as tetrahydrate or monohydrate or sodium percarbonate. These can be present in proportions of up to 30% by weight, preferably 5 to 25% by weight.
- the preferred oxygen carrier is sodium perborate monohydrate, the proportion of which can be up to 20% by weight, preferably 5 to 15% by weight.
- the detergents can also contain conventional detergent additives as further constituents, such as optical brighteners, graying inhibitors, disinfectant substances and colorants and fragrances.
- Suitable graying inhibitors are carboxymethyl cellulose (sodium salt), methyl cellulose, hydroxyalkyl cellulose and mixed ethers such as methyl hydroxyethyl cellulose and mixtures of the cellulose ethers mentioned.
- the proportion of graying inhibitors is generally up to 3% by weight, usually 0.5 to 2% by weight.
- the proportion of the other additives is generally less than 1% by weight, usually less than 0.5% by weight.
- the moldings or blocks can be produced in such a way that the surfactants and the polyethers (components C and D) are melted in heated kneading machines or pilier devices or are introduced in an already molten state, whereupon the other components are in fine powdered or granular form adds and homogenizes the plastic mixture.
- the grain size of the solid additives is not critical per se, which is why it is not necessary to grind these additives beforehand to a fineness of dust. In the interest of easy homogenizability and a reduction in the need for plasticizers, however, it has proven expedient if the solids have no significant proportions with a grain size above 1.6 mm, in particular no proportions above 1.2 mm. Average grain sizes from 0.05 to 0.8 mm are therefore well suited.
- the temperature of the melt can be 40 ° to 100 ° C. In the interest of reducing the viscosity of the mixtures, however, minimum temperatures of 60 ° C., advantageously those of 75 ° to 90 ° C. prefers.
- the viscosity in this range should not exceed 50,000 mPa.s, or at least not significantly. If active oxygen-containing compounds are incorporated, the temperature should preferably not exceed 80 ° C. and the mixture should then be cooled and solidified as quickly as possible in order to avoid unnecessary loss of oxygen.
- the homogenized melt can be pressed into strands while cooling, which can then be cut, as is customary in soap processing, and further deformed under pressure. However, they can also be advantageously poured into molds from which they can be easily ejected after cooling to temperatures below 40 ° C. This simple working method benefits from the fact that in many cases the moldings are sufficiently dimensionally stable even at this temperature.
- the shape of the shaped body can be any, for. B. cylindrical, cuboid or of round or oval shape. Pieces formed by solidification advantageously have the shape of a truncated cone, truncated pyramid or a cuboid with a reduced base area up to hemispherical shapes for easier removal from the casting mold. With a formulation-dependent density of 1.3 to 1.7 g / cm3, the amount or size of the shaped body required for a washing process can be adjusted in a simple manner.
- the unit weight for a washing process in a commercial washing machine is of the order of 300 g.
- the type of flushing can also be carried out in various ways and adapted to the properties of the moldings or the existing washing technology.
- the entire water supply is passed through the induction chamber and then the wash liquor is circulated through the chamber until the desired concentration is reached. This concentration can be determined and programmed using the electrical conductivity of the wash liquor.
- a similar procedure can be followed if large moldings intended for multiple washing processes are used.
- a partial flow can be branched off from the water inlet and passed through the induction chamber.
- the rate of dissolution can then also be influenced via the temperature of the water supplied. Molded portions portioned for a wash cycle or existing product residues can be melted and flushed in very quickly by adding hot water from a mixer tap with steam supply. A conductivity check of the wash liquor concentration is not necessary.
- a concept deviating from the dissolving chamber which offers a number of advantages, is a device which is placed on the induction chamber or integrated therein and mechanically comminutes the detergent block to form a free-flowing powder.
- the grinder is e.g. B. electrically driven and supports the block in layers, e.g. B. by means of a rotating or vibrating grater.
- the mechanical dosing chamber advantageously has a capacity of several vertically stacked moldings which pass through the shredding area one after the other.
- the detergent dosing can be carried out via conductivity control in the washing liquor or, more simply, via the one switching duration of the grater can be controlled.
- a water jet rinses the powder from the dispenser into the washing machine.
- meltable formulation components C and D given in the tables were combined in a heatable kneader and melted at temperatures between 80 and 100.degree.
- the solid constituents, which had a particle size of 0.05 to 0.5 mm, were then added and the melt was homogenized. If sodium perborate was added, the melt was previously cooled to 80 ° C. After complete homogenization, the molten mass was poured into cylindrical molds and quickly cooled to room temperature. Analytical tests showed that no separation or settling of individual grain fractions had taken place in the casting mold during cooling.
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Abstract
Description
Die Erfindung betrifft ein Waschmittel, das insbesondere zur Verwendung in gewerblichen Wäschereien bestimmt ist. Diese Wäschereien verwenden üblicherweise enthärtetes Wasser, weshalb der Gehalt der Waschmittel an Kalkhärte bindenden Buildersalzen gegenüber einem Haushaltswaschmittel vergleichsweise niedrig ist, während der Gehalt an stark alkalischen Buildersalzen, insbesondere Metasilikaten, üblicherweise sehr viel höher liegt. Aufgrund der hohen Alkalität erfordern pulverförmige Mittel bei ihrer Handhabung sowie wegen der Tendenz, bei Feuchtigkeitseinwirkung zu verklumpen, besondere Vorsichtsmaßnahmen. Es ist zwar bekannt, daß man derartige Mittel auch als flüssige Konzentrate, sogenannte Stammlaugen, bevorraten und dosieren kann, jedoch eignen sich die dafür benötigten technischen Anlagen wegen ihres erhöhten Aufwandes und Platzbedarfes nicht für jeden Standort.The invention relates to a detergent which is intended in particular for use in commercial laundries. These laundries usually use softened water, which is why the detergent content of builder salts that bind the hardness of lime is comparatively low compared to a household detergent, while the content of strongly alkaline builder salts, in particular metasilicates, is usually much higher. Due to the high level of alkalinity, powdery agents require special precautions when handling them and because they tend to clump together when exposed to moisture. Although it is known that such agents can also be stored and metered as liquid concentrates, so-called stock lyes, the technical systems required for this are not suitable for every location because of their increased expenditure and space requirements.
Es bestand daher die Aufgabe, ein derartiges Mittel in einer bequem handhabbaren, leicht und verlustfrei zu dosierenden Form anzubieten. Als geeignete Form bietet sich die Tabletten-, Stück- oder Blockform an. Für diese Anbietungsform ist zusätzlich zu fordern, daß die Mittel schnell und vollständig in der Einspülvorrichtung der Waschmaschinen gelöst werden, um kurze Arbeitstakte zu ermöglichen. Andererseits müssen derartige Stücke, anders als bei Pulverpreßlingen, gegen mechanische Beanspruchung hinreichend stabil und so kompakt sein, daß eine schichtweise, gleichmäßige Auflösung ohne Zerfall des Formkörpers ermöglicht wird. Zerfallende Pulverpreßlinge verursachen häufig harte Anbackungen in den Einspülkästen.It was therefore the task of offering such an agent in a conveniently manageable, light and loss-free dosage form. The tablet, piece or block form is a suitable form. For this form of supply, it is additionally required that the agents be dissolved quickly and completely in the washing-up device of the washing machines in order to enable short work cycles. On the other hand, unlike powder compacts, pieces of this type must be sufficiently stable against mechanical stress and so compact that layer-by-layer, uniform dissolution without disintegration of the shaped body enables them becomes. Crumbling powder compacts often cause hard deposits in the induction boxes.
Gegenstand der Erfindung, mit denen diese Aufgaben gelöst werden, ist ein Waschmittel in Form von schmelzbaren Formkörper, enthaltend (als wasserfreie Substanz gerechnet):
- A) 35 bis 65 Gew.-% Natriummetasilikat,
- B) 4 bis 25 Gew.-% mindestens eine polyanionische Buildersubstanz aus der Klasse der Polyphosphate, Zeolithe, der Nitrilotriessigsäure, der (co-)polymeren Carbonsäuren und der Polyphosphonsäuren, jeweils in Form der Natriumsalze,
- C) 10 bis 30 Gew.-% eines nichtionischen Tensids,
- D) 2 bis 15 Gew.-% einer wasserlöslichen, wachsartigen Verbindung aus der Klasse der Polyethylenglykole mit einem Molekulargewicht von mindestens 1100 und deren Alkylether.
- A) 35 to 65% by weight sodium metasilicate,
- B) 4 to 25% by weight of at least one polyanionic builder from the class of the polyphosphates, zeolites, nitrilotriacetic acid, the (co) polymeric carboxylic acids and the polyphosphonic acids, in each case in the form of the sodium salts,
- C) 10 to 30% by weight of a nonionic surfactant,
- D) 2 to 15% by weight of a water-soluble, waxy compound from the class of polyethylene glycols with a molecular weight of at least 1100 and their alkyl ethers.
Das Natriummetasilikat (Komponente A) der Zusammensetzung Na₂O:SiO₂ = 1:0,9 bis 1:1,1 kommt als wasserfreie Substanz zum Einsatz. Die bevorzugte Menge beträgt 40 bis 60 Gew.-% und insbesondere 45 bis 55 Gew.-%.The sodium metasilicate (component A) with the composition Na₂O: SiO₂ = 1: 0.9 to 1: 1.1 is used as an anhydrous substance. The preferred amount is 40 to 60% by weight and in particular 45 to 55% by weight.
Die Komponente (B) besteht aus mindestens einem polyanionischen Buildersalz aus der Klasse der Polyphosphate, der Nitrilotriessigsäure, des Zeoliths, der Polyphosphonsäuren und der (co-)polymeren Carbonsäuren in Form der Natriumsalze. Ihr Anteil beträgt insgesamt 4 bis 25 Gew.-%, vorzugsweise 5 bis 20 Gew.-% und insbesondere 7 bis 15 Gew.-%.Component (B) consists of at least one polyanionic builder salt from the class of the polyphosphates, nitrilotriacetic acid, zeolite, polyphosphonic acids and (co) polymeric carboxylic acids in the form of the sodium salts. Their total amount is 4 to 25% by weight, preferably 5 to 20% by weight and in particular 7 to 15% by weight.
Als Polyphosphat kommt in erster Linie Natriumtripolyphosphat (TPP) in Frage, das in Anteilen von 0 bis 10 Gew.-%, vorzugsweise 0 bis 5 Gew.-% anwesend sein kann. Selbstverständlich sind in Fällen, in denen phosphatfreie Mittel zwingend vorgeschrieben sind, auch TPP-freie Mittel geeignet. In diesen Fällen besteht die Komponente (B) zweckmäßigerweise aus Nitrilotriacetat (NTA) oder Zeolith oder NTA-Zeolith-Gemischen oder aus Zeolith im Gemisch mit (co-)polymeren Carbonsäuren, die als sogenannte Co-Builder und Threshold-Wirkstoffe agieren. Auch Polyphosphonate besitzen in Kombination mit Zeolith diese Eigenschaften.The most suitable polyphosphate is sodium tripolyphosphate (TPP), which can be present in proportions of 0 to 10% by weight, preferably 0 to 5% by weight. Of course, in cases where phosphate-free agents are mandatory are also suitable TPP-free agents. In these cases, component (B) advantageously consists of nitrilotriacetate (NTA) or zeolite or NTA-zeolite mixtures or of zeolite in a mixture with (co) polymeric carboxylic acids which act as so-called co-builders and threshold active ingredients. In combination with zeolite, polyphosphonates also have these properties.
NTA als Phosphatsubstitut kann in Mengen von 0 bis 7, vorzugsweise 0 bis 6 und insbesondere 0 bis 5 Gew.-% eingesetzt werden. Diese Mengen beziehen sich auf wasserfreies Trinatriumsalz.NTA as a phosphate substitute can be used in amounts of 0 to 7, preferably 0 to 6 and in particular 0 to 5% by weight. These amounts refer to anhydrous trisodium salt.
Bevorzugte Phosphatsubstitute sind feinkristalline, synthetische, wasserhaltige Zeolithen vom Typ NaA, die ein Calciumbindevermögen im Bereich von 100 bis 200 mg CaO/g (gemäß den Angaben in DE 22 24 837) aufweisen. Ihre Teilchengröße liegt üblicherweise im Bereich von 1 bis 10 µm. Der Gehalt an diesen Zeolithen beträgt 0 bis 15, vorzugsweise 0 bis 10 Gew.-%. Mittel ohne Phosphat bzw. ohne NTA enthalten zweckmäßigerweise 5 bis 10 Gew.-% Zeolith.Preferred phosphate substitutes are finely crystalline, synthetic, water-containing zeolites of the NaA type, which have a calcium binding capacity in the range from 100 to 200 mg CaO / g (according to the information in DE 22 24 837). Their particle size is usually in the range from 1 to 10 μm. The content of these zeolites is 0 to 15, preferably 0 to 10% by weight. Agents without phosphate or without NTA advantageously contain 5 to 10% by weight of zeolite.
Der Zeolith wird vorzugsweise zusammen mit polyanionischen Co-Buildern verwendet. Hierzu zählen Verbindungen aus der Klasse der Polyphosphonsäuren sowie der homo- bzw. copolymeren Polycarbonsäuren, abgeleitet von Acrylsäure, Methacrylsäure, Maleinsäure und olefinischen ungesättigten, copolymerisierbaren Verbindungen.The zeolite is preferably used together with polyanionic co-builders. These include compounds from the class of polyphosphonic acids and homo- or copolymeric polycarboxylic acids, derived from acrylic acid, methacrylic acid, maleic acid and olefinic unsaturated, copolymerizable compounds.
Geeignete Phosphonsäuren bzw. phosphonsaure Salze 1-Hydroxyethan-1,1-diphosphonat, Ethylendiamin-tetramethylenphosphonat (EDTMP) und Diethylentriamin-pentamethylenphosphonat, meist in Form ihrer Natriumsalze sowie ihre Gemische eingesetzt. Die Mengen betragen üblicherweise bis 2,0 Gew.-%, bezogen auf die Mittel, vorzugsweise 0,2 bis 1 Gew.-%, bezogen auf Natriumsalz. Im Falle des Diphosphonates bezieht sich diese Menge auf das Tri natriumsalz, im Falle des Tetraphosphonats auf das Hexanatriumsalz.Suitable phosphonic acids or phosphonic acid salts 1-hydroxyethane-1,1-diphosphonate, ethylenediamine tetramethylene phosphonate (EDTMP) and diethylenetriamine pentamethylene phosphonate, mostly in the form of their sodium salts and their mixtures. The amounts are usually up to 2.0% by weight, based on the composition, preferably 0.2 to 1% by weight, based on the sodium salt. In the case of the diphosphonate, this amount refers to the tri sodium salt, in the case of tetraphosphonate on the hexasodium salt.
Weitere brauchbare Co-Builder sind Homopolymere der Acrylsäure und der Methacrylsäure, Copolymere der Acrylsäure mit Methacrylsäure und Copolymere der Acrylsäure, Methacrylsäure oder Maleinsäure mit Vinylethern, wie Vinylmethylether beziehungsweise Vinylethylether, ferner mit Vinylestern, wie Vinylacetat oder Vinylpropionat, Acrylamid, Methacrylamid sowie mit Ethylen, Propylen oder Styrol. In solchen copolymeren Säuren, in denen eine der Komponenten keine Säurefunktion aufweist, beträgt deren Anteil im Interesse einer ausreichenden Wasserlöslichkeit nicht mehr als 70 Molprozent, vorzugsweise weniger als 60 Molprozent. Als besonders geeignet haben sich Copolymere der Acrylsäure beziehungsweise Methacrylsäure mit Maleinsäure erwiesen, wie sie beispielsweise in EP 25 551-B 1 charakterisiert sind. Es handelt sich dabei um Copolymerisate, die 40 bis 90 Gewichtsprozent Acrylsäure enthalten. Besonders bevorzugt sind solche Copolymere, in denen 50 bis 85 Gewichtsprozent Acrylsäure und 50 bis 15 Gew.-% Maleinsäure vorliegen.Further useful co-builders are homopolymers of acrylic acid and methacrylic acid, copolymers of acrylic acid with methacrylic acid and copolymers of acrylic acid, methacrylic acid or maleic acid with vinyl ethers, such as vinyl methyl ether or vinyl ethyl ether, furthermore with vinyl esters, such as vinyl acetate or vinyl propionate, acrylamide, methacrylamide and with ethylene, Propylene or styrene. In those copolymeric acids in which one of the components has no acid function, the proportion thereof in the interest of sufficient water solubility is not more than 70 mole percent, preferably less than 60 mole percent. Copolymers of acrylic acid or methacrylic acid with maleic acid, as are characterized, for example, in EP 25 551-B 1, have proven to be particularly suitable. These are copolymers which contain 40 to 90 percent by weight of acrylic acid. Copolymers in which 50 to 85% by weight of acrylic acid and 50 to 15% by weight of maleic acid are present are particularly preferred.
Die genannten (co-)polymeren Carbonsäuren können auch ohne Mitverwendung von Zeolithen eingesetzt werden. In derartigen Fällen kann ihr Anteil bis zu 7 Gew.-%, vorzugsweise bis 6 Gew.-% betragen, bezogen auf neutral reagierendes, d. h. in wäßriger Lösung einen pH-Wert von 7 bis 8 aufweisendes Natriumsalz. In zeolithhaltigen Produkten kann ihr Anteil reduziert werden, beispielsweise auf Anteile bis 6 %, vorzugsweise 0,5 bis 5 Gew.-% und insbesondere 1 bis 4 Gew.-%.The (co) polymeric carboxylic acids mentioned can also be used without the use of zeolites. In such cases, their proportion can be up to 7% by weight, preferably up to 6% by weight, based on neutral reacting, i.e. H. in aqueous solution having a pH of 7 to 8 sodium salt. In zeolite-containing products, their proportion can be reduced, for example to proportions up to 6%, preferably 0.5 to 5% by weight and in particular 1 to 4% by weight.
Als nichtionische Tenside (Komponente C) sind Anlagerungsprodukte von 2 bis 20, vorzugsweise 3 bis 15 Mol Ethylenoxid (EO) an 1 Mol einer Verbindung mit im wesentlichen 10 bis 20 Kohlenstoffatomen aus der Gruppe der Alkohole verwendbar. Geeignete nichtionische Tenside leiten sich von primären Alkoholen, wie z.B. an Kokos- oder Talgfettalkohole, Oleylalkohol, Oxoalkohole, oder an sekundären Alkoholen mit 8 bis 18, vorzugsweise 12 bis 18 C-Atomen ab. Bevorzugt werden Kombinationen von wasserlöslichen nichtionischen Tensiden (Komponente C1) und wasserunlöslichen bzw. in Wasser dispergierbaren nichtionischen Tensiden (Komponente C2) eingesetzt. Zur Komponente C1 zählen solche mit 6 bis 15 EO und einem HLB-Wert von mehr als 11, zur Komponente C2 solche mit 2 bis 6 EO und einem HLB-Wert von 11 oder weniger. Das Verhältnis von C1 zu C2 kann 2:1 bis 1:4 betragen, vorzugsweise 1:1 bis 1:3.Addition products of 2 to 20, preferably 3 to 15 moles of ethylene oxide (EO) with 1 mole of a compound having essentially 10 to 20 carbon atoms from the group of the alcohols can be used as nonionic surfactants (component C). Suitable nonionic surfactants are derived from primary alcohols, e.g. on coconut or tallow fatty alcohols, oleyl alcohol, oxo alcohols, or on secondary alcohols with 8 to 18, preferably 12 to 18 carbon atoms. Combinations of water-soluble nonionic surfactants (component C1) and water-insoluble or water-dispersible nonionic surfactants (component C2) are preferably used. Component C1 includes those with 6 to 15 EO and an HLB value of more than 11, component C2 includes those with 2 to 6 EO and an HLB value of 11 or less. The ratio of C1 to C2 can be 2: 1 to 1: 4, preferably 1: 1 to 1: 3.
Die nichtionischen Tenside können auch Propylenglykolether-Gruppen (PO) aufweisen. Diese können endständig angeordnet oder statistisch mit den EO-Gruppen verteilt sein. Bevorzugte Verbindungen dieser Klasse sind solche vom Typ R-(PO)x-(EO)y, worin R für den hydrophoben Rest steht, x Zahlen von 0,5 bis 3 und y Zahlen von 3 bis 20 bedeuten.The nonionic surfactants can also have propylene glycol ether groups (PO). These can be arranged at the end or distributed statistically with the EO groups. Preferred compounds of this class are those of the type R- (PO) x - (EO) y , in which R is the hydrophobic radical, x are numbers from 0.5 to 3 and y numbers from 3 to 20.
Als nichtionische Tenside kommen gegebenenfalls auch Ethoxylate von Alkylphenolen, 1,2-Diolen, Fettsäuren und Fettsäureamiden sowie Blockpolymere aus Polypropylenglykol und Polyethylenglykol bzw. alkoxylierten Alkylendiaminen (Typ Pluronics und Tetronics) in Betracht. Weiterhin lassen sich die vorbeschriebenen nichtionischen Tenside vom EO-Typ teilweise durch Alkylpolyglycoside ersetzen. Geeignete Alkylpolyglycoside weisen beispielsweise einen C₈₋₁₆-Alkylrest und einen oligomeren Glycosidrest mit 1,5 bis 6 Glucosegruppen auf. Tenside vom Alkylglycosid-Typ sind vorzugsweise mit nichtionischen Ethoxylat-Tensiden kombiniert, beispielsweise im Verhältnis 5:1 bis 1:5.Other suitable nonionic surfactants are ethoxylates of alkylphenols, 1,2-diols, fatty acids and fatty acid amides and block polymers of polypropylene glycol and polyethylene glycol or alkoxylated alkylenediamines (Pluronics and Tetronics type). Furthermore, the above-described nonionic surfactants of the EO type can be partially replaced by alkyl polyglycosides. Suitable alkyl polyglycosides have, for example, a C₈₋₁₆ alkyl radical and an oligomeric glycoside radical with 1.5 to 6 glucose groups. Alkyl glycoside-type surfactants are preferably combined with nonionic ethoxylate surfactants, for example in a ratio of 5: 1 to 1: 5.
Der Gehalt der Mittel an nichtionischen Tensiden bzw. nichtionischen Tensidgemischen beträgt 10 bis 30 Gew.-%, vorzugsweise 15 bis 25 Gew.-% und insbesondere 18 bis 22 Gew.-%.The content of the agents in nonionic surfactants or nonionic surfactant mixtures is 10 to 30% by weight, preferably 15 to 25% by weight and in particular 18 to 22% by weight.
Die Mittel können gegebenenfalls auch anionische Tenside enthalten, die als Komponente E bezeichnet werden. Geeignet sind Seifen und Tenside vom Sulfonat- bzw. Sulfat-Typ. Anteile bis zu 5 Gew.-%, in einzelnen Fällen bis 10 Gew.-% an anionischen Tensiden erhöhen die Waschleistung, führen jedoch meist zu einer unerwünschten Schaumaktivität. Diese Schaumaktivität kann durch Zusatz geeigneter Schauminhibitoren reduziert werden. Geeignet sind Organopolysilixane, insbesondere Polydimethylsiloxane sowie deren Gemische mit Kieselsäure bzw. silanierter Kieselsäure, Kohlenwasserstofföle und -wachse, mikrokristalline Wachse und von C₂₋₆Alkylendiaminen abgeleitete Bis-acyl-alkylendiamine mit langkettigen, 14 bis 22 C-Atome aufweisenden Acylresten (Fettsäure-resten). Vorteilhaft werden auch Gemische derartiger Schauminhibitoren verwendet. Der Gehalt der Mittel an derartigen Schauminhibitoren hängt von der Menge und der Schaumaktivität der synthetischen anionischen Tenside ab und beträgt bis zu 5 Gew.-%, vorzugsweise 0,5 bis 3 Gew.-%, bezogen auf anionisches Tensid.The agents can optionally also contain anionic surfactants, which are referred to as component E. Soaps and surfactants of the sulfonate or sulfate type are suitable. Contents of up to 5% by weight, in some cases up to 10% by weight, of anionic surfactants increase the washing performance, but usually lead to an undesirable foam activity. This foam activity can be reduced by adding suitable foam inhibitors. Organopolysilixanes, in particular polydimethylsiloxanes and mixtures thereof with silica or silanized silica, hydrocarbon oils and waxes, microcrystalline waxes and bis-acylalkylenediamines derived from C₂ abgelalkylenediamines with long-chain acyl residues containing 14 to 22 carbon atoms (fatty acid residues) are suitable . Mixtures of such foam inhibitors are also advantageously used. The amount of such foam inhibitors in the compositions depends on the amount and the foam activity of the synthetic anionic surfactants and is up to 5% by weight, preferably 0.5 to 3% by weight, based on the anionic surfactant.
Geeignete Seifen leiten sich von natürlichen oder synthetischen, gesättigten oder einfach ungesättigten Fettsäuren mit 12 bis 22 C-Atomen ab. Geeignet sind insbesondere aus natürlichen Fettsäuren, z. B. Kokos-, Palmkern- oder Talgfettsäuren abgeleitete Seifengemische. Bevorzugt sind solche, die zu 50 bis 100 % aus gesättigten C₁₂₋₁₈-Fettsäureseifen und zu 0 bis 50 % aus Ölsäureseife zusammengesetzt sind. Ihr Anteil kann bis 10 Gew.-%, vorzugsweise bis 4 Gew.-% betragen, bezogen auf Natriumseifen.Suitable soaps are derived from natural or synthetic, saturated or monounsaturated fatty acids with 12 to 22 carbon atoms. Are particularly suitable from natural fatty acids such. B. coconut, palm kernel or tallow fatty acid derived soap mixtures. Preferred are those which are composed of 50 to 100% of saturated C₁₂₋₁₈ fatty acid soaps and 0 to 50% of oleic acid soap. Their proportion can be up to 10% by weight, preferably up to 4% by weight, based on sodium soaps.
Brauchbare Tenside vom Sulfonattyp sind lineare Alkylbenzolsulfonate (C₉₋₁₃-Alkyl) und Olefinsulfonate, d. h. Gemische aus Alken- und Hydroxylalkansulfonaten sowie Disulfonaten, wie man sie beispielsweise aus C₁₂₋₁₈-Monoolefinen mit end- oder innenständiger Doppelbindung durch Sulfonieren mit gasförmigem Schwefeltrioxid und anschließende alkalische Hydrolyse der Sulfonierungsprodukte erhält. Geeignet sind auch Alkansulfonate, die aus C₁₂₋₁₈-Alkanen durch Sulfochlorierung oder Sulfooxydation und anschließende Hydrolyse bzw. Neutralisation erhältlich sind, sowie alphasulfonierte hydrierte Kokos-, Palmkern- oder Talgfettsäuren und deren Methyl- oder Ethylester sowie deren Gemische. Unter den Sulfonatgruppen enthaltenden Tenside sind bevorzugt die Alkylbenzolsulfonate, Alpha-Sulfofettsäureestersalze und die Alpha-Sulfofettsäureester-disalze. Sie liegen in Form ihrer Natriumsalze vor. Ihr Anteil kann bis 5 Gew.-%, in einzelnen Fällen bis 8 Gew.-% betragen. Vorzugsweise beträgt er maximal 2 Gew.-%.Usable surfactants of the sulfonate type are linear alkylbenzenesulfonates (C₉₋₁₃-alkyl) and olefin sulfonates, ie mixtures of alkene and hydroxylalkanesulfonates as well as disulfonates, as can be obtained, for example, from C₁₂₋₁inen monoolefins with a terminal or internal double bond by sulfonating with gaseous sulfur trioxide and subsequent receives alkaline hydrolysis of the sulfonation products. Alkanesulfonates made from C₁₂₋₁₈ alkanes by sulfochlorination or sulfo-oxidation and subsequent hydrolysis or neutralization are available, and alphasulfonated hydrogenated coconut, palm kernel or tallow fatty acids and their methyl or ethyl esters and mixtures thereof. Among the surfactants containing sulfonate groups, preference is given to the alkylbenzenesulfonates, alpha-sulfofatty acid ester salts and the alpha-sulfofatty acid ester disalts. They are in the form of their sodium salts. Their proportion can be up to 5% by weight, in some cases up to 8% by weight. It is preferably at most 2% by weight.
Als Bindemittel (Komponente D) enthalten die Mittel 2 bis 15 Gew.-%, bevorzugt 2 bis 10 Gew.-% und insbesondere 3 bis 8 Gew.-% an wasserlöslichen, wachsartigen Verbindungen aus der Klasse der Polyäthylenglykole mit einem Molekulargewicht von mindestens 1100 sowie deren Alkylether. Vorzugsweise beträgt das Molekulargewicht des Polyglykolethers 1300 bis 40 000 und, sofern er keine Alkylgruppen aufweist, insbesondere 1500 bis 20000. In den alkylsubstituierten Polyglykolethern kann die Alkylkette 6 bis 24 C-Atome, vorzugsweise 10 bis 18 C-Atome aufweisen. Als besonders gut geeignet haben sich von C₁₄₋₁₈-Alkoholen bzw. Alkoholgemischen (z. B. Talgalkohol) abgeleitete Alkylpolyglykolether erwiesen, die 25 bis 100, vorzugsweise 30 bis 50 Ethylenglykolethergruppen aufweisen. Unsubstituierte und alkylsubstituierte Polyether können auch im Gemisch vorliegen.The binders (component D) contain 2 to 15% by weight, preferably 2 to 10% by weight and in particular 3 to 8% by weight, of water-soluble, wax-like compounds from the class of polyethylene glycols with a molecular weight of at least 1100 and their alkyl ethers. The molecular weight of the polyglycol ether is preferably from 1300 to 40,000 and, if it has no alkyl groups, in particular from 1500 to 20,000. In the alkyl-substituted polyglycol ethers, the alkyl chain can have 6 to 24 C atoms, preferably 10 to 18 C atoms. Alkyl polyglycol ethers derived from C₁₄₋₁₈ alcohols or alcohol mixtures (for example tallow alcohol) which have 25 to 100, preferably 30 to 50, ethylene glycol ether groups have proven particularly suitable. Unsubstituted and alkyl-substituted polyethers can also be present in a mixture.
Als weitere Komponente F können die Mittel auch Aktivsauerstoff enthaltende Verbindungen enthalten, wie Natriumperborat als Tetrahydrat oder Monohydrat oder Natriumpercarbonat. Diese können in Anteilen bis zu 30 Gew.-%, vorzugsweise 5 bis 25 Gew.-% anwesend sein. Bevorzugter Sauerstoffträger ist Natriumperborat-Monohydrat, dessen Anteil bis 20 Gew.-%, vorzugsweise 5 bis 15 Gew.-% betragen kann. Überraschend hat sich gezeigt, daß derartige, in hochalkalischen Gemischen normalerweise instabilen Perverbindungen nach dem Inkorporieren in die erfindungsgemäßen Mittel außerordentlich lagerbeständig sind und beispielsweise nach 6monatiger Lagerung bei 25 °C noch keinen meßbaren Sauerstoffverlust erleiden.As further component F, the agents can also contain compounds containing active oxygen, such as sodium perborate as tetrahydrate or monohydrate or sodium percarbonate. These can be present in proportions of up to 30% by weight, preferably 5 to 25% by weight. The preferred oxygen carrier is sodium perborate monohydrate, the proportion of which can be up to 20% by weight, preferably 5 to 15% by weight. Surprisingly, it has been found that such per-compounds, which are normally unstable in highly alkaline mixtures, after incorporation into the inventive compounds Medium are extraordinarily stable and, for example, after 6 months of storage at 25 ° C., do not yet suffer any measurable loss of oxygen.
Als weitere Bestandteile können die Mittel noch übliche Waschmittelzusätze enthalten, wie optische Aufheller, Vergrauungsinhibitoren, desinfizierend wirkende Stoffe sowie Farb- und Duftstoffe. Als Vergrauungsinhibitoren kommen Carboxymethylcellulose (Na-Salz), Methylcellulose, Hydroxyalkylcellulose sowie Mischether, wie Methylhydroxyethylcellulose sowie Gemische der genannten Celluloseether in Betracht. Der Anteil der Vergrauungsinhibitoren beträgt im allgemeinen bis zu 3 Gew.-%, meist 0,5 bis 2 Gew.-%. Der Anteil der übrigen Zusätze liegt im allgemeinen unter 1 Gew.-%, meist unter 0,5 Gew.-%.The detergents can also contain conventional detergent additives as further constituents, such as optical brighteners, graying inhibitors, disinfectant substances and colorants and fragrances. Suitable graying inhibitors are carboxymethyl cellulose (sodium salt), methyl cellulose, hydroxyalkyl cellulose and mixed ethers such as methyl hydroxyethyl cellulose and mixtures of the cellulose ethers mentioned. The proportion of graying inhibitors is generally up to 3% by weight, usually 0.5 to 2% by weight. The proportion of the other additives is generally less than 1% by weight, usually less than 0.5% by weight.
Die Herstellung der Formstücke bzw. Blöcke kann in der Weise erfolgen, daß man in beheizbaren Knetmaschinen oder Piliervorrichtungen die Tenside und die Polyether (Komponenten C und D) aufschmilzt oder in bereits geschmolzenem Zustand vorlegt, worauf man die übrigen Komponenten in feinpulvriger oder auch granulierter Form zufügt und das plastische Gemisch homogenisiert. Die Korngröße der festen Zusätze ist an sich nicht kritisch, weshalb es auch nicht erforderlich ist, diese Zusätze zuvor auf Staubfeinheit zu vermahlen. Im Interesse einer leichten Homogenisierbarkeit und einer Reduzierung des Bedarfes an Plastifiziermittel hat es sich jedoch als zweckmäßig erwiesen, wenn die Feststoffe keine nennenswerten Anteile mit einer Korngröße oberhalb 1,6 mm, insbesondere keine Anteile oberhalb 1,2 mm aufweisen. Mittlere Korngrößen von 0,05 bis 0,8 mm sind daher gut geeignet.The moldings or blocks can be produced in such a way that the surfactants and the polyethers (components C and D) are melted in heated kneading machines or pilier devices or are introduced in an already molten state, whereupon the other components are in fine powdered or granular form adds and homogenizes the plastic mixture. The grain size of the solid additives is not critical per se, which is why it is not necessary to grind these additives beforehand to a fineness of dust. In the interest of easy homogenizability and a reduction in the need for plasticizers, however, it has proven expedient if the solids have no significant proportions with a grain size above 1.6 mm, in particular no proportions above 1.2 mm. Average grain sizes from 0.05 to 0.8 mm are therefore well suited.
Die Temperatur der Schmelze kann, je nach Schmelzbereich der Komponenten C und D, 40° bis 100°C betragen. Im Interesse einer Herabsetzung der Viskosität der Gemische sind jedoch Mindesttemperaturen von 60°C, vorteilhaft solche von 75° bis 90°C bevorzugt. Die Viskosität in diesem Bereich sollte 50 000 mPa.s nicht oder zumindest nicht wesentlich übersteigen. Sofern Aktivsauerstoff enthaltende Verbindungen eingearbeitet werden, soll die Temperatur vorzugsweise 80 °C nicht überschreiten und das Gemisch anschließend möglichst schnell abgekühlt und zum Erstarren gebracht werden, um einen unnötigen Sauerstoffverlust zu vermeiden.The temperature of the melt, depending on the melting range of components C and D, can be 40 ° to 100 ° C. In the interest of reducing the viscosity of the mixtures, however, minimum temperatures of 60 ° C., advantageously those of 75 ° to 90 ° C. prefers. The viscosity in this range should not exceed 50,000 mPa.s, or at least not significantly. If active oxygen-containing compounds are incorporated, the temperature should preferably not exceed 80 ° C. and the mixture should then be cooled and solidified as quickly as possible in order to avoid unnecessary loss of oxygen.
Die homogenisierte Schmelze kann unter Abkühlung zu Strängen verpreßt werden, die anschließend, wie in der Seifenverarbeitung üblich, zerschnitten und unter Druck weiter verformt werden können. Mit Vorteil lassen sie sich aber auch in Formen gießen, aus denen sie sich nach dem Abkühlen auf Temperaturen unterhalb 40°C leicht ausstoßen lassen. Dieser einfachen Arbeitsweise kommt es zugute, daß die Formkörper in vielen Fällen schon bei dieser Temperatur ausreichend formstabil sind.The homogenized melt can be pressed into strands while cooling, which can then be cut, as is customary in soap processing, and further deformed under pressure. However, they can also be advantageously poured into molds from which they can be easily ejected after cooling to temperatures below 40 ° C. This simple working method benefits from the fact that in many cases the moldings are sufficiently dimensionally stable even at this temperature.
Die Gestalt der Formkörper kann beliebig sein, z. B. zylindrisch, quaderförmig oder auch von rundlicher bzw. ovaler Form. Durch Erstarrenlassen geformte Stücke weisen zwecks erleichterter Entnahme aus der Gießform vorteilhaft die Form eines Kegelstumpfes, Pyramidenstumpfes oder eines Quaders mit verkleinerter Basisfläche bis hin zu halbkugeligen Formen auf. Bei einer rezepturabhängigen Dichte von 1,3 bis 1,7 g/cm³ läßt sich auf diese Weise die für einen Waschprozeß benötigte Menge bzw. Größe des Formkörpers in einfacher Weise einstellen. Das Stückgewicht liegt bei einem Waschprozeß in einer kommerziellen Waschmaschine in der Größenordnung von 300 g. Man kann jedoch auch größere Stücke in den Einspülvorrichtungen deponieren und die zu lösende Menge bzw. die gewünschte Laugenkonzentration durch Bestimmung der elektrischen Leitfähigkeit regulieren. Da der vordosierte Formkörper nicht dazu neigt, sich unter Krustenbildung in der Einspülvorrichtung festzusetzen, lassen sich mehrere Waschvorgänge mit einer einmaligen Dosierung bewerkstelligen und die Bedienung der Anlage rationalisieren.The shape of the shaped body can be any, for. B. cylindrical, cuboid or of round or oval shape. Pieces formed by solidification advantageously have the shape of a truncated cone, truncated pyramid or a cuboid with a reduced base area up to hemispherical shapes for easier removal from the casting mold. With a formulation-dependent density of 1.3 to 1.7 g / cm³, the amount or size of the shaped body required for a washing process can be adjusted in a simple manner. The unit weight for a washing process in a commercial washing machine is of the order of 300 g. However, larger pieces can also be deposited in the induction devices and the amount to be dissolved or the desired alkali concentration can be regulated by determining the electrical conductivity. Since the pre-dosed shaped body does not tend to become stuck in the induction device with crust formation, several washing processes can be carried out manage with a single dose and rationalize the operation of the system.
Auch die Art des Einspülens kann in verschiedener Weise durchgeführt und den Eigenschaften der Formkörper bzw. der vorhandenen Waschtechnik angepaßt werden. Bei Formkörpern mit niedriger Lösungsgeschwindigkeit leitet man den gesamten Wasserzulauf durch die Einspülkammer und führt anschließend die Waschlauge im Kreislauf durch die Kammer, bis die gewünschte Konzentration erreicht ist. Diese Konzentration kann mit Hilfe der elektrischen Leitfähigkeit der Waschlauge ermittelt und programmiert werden. In ähnlicher Weise kann man verfahren, wenn man große, für mehrere Waschvorgänge bestimmte Formkörper einsetzt. Für Formkörper mit hoher Lösegeschwindigkeit kann ein Teilstrom vom Wasserzulauf abgezweigt und durch die Einspülkammer geführt werden. Die Lösegeschwindigkeit kann dann zusätzlich über die Temperatur des zugeführten Wassers beeinflußt werden. Für einen Waschgang portionierte Formkörper oder auch vorhandene Produktreste können in kürzester Zeit durch Zuführung von Heißwasser aus einer Mischbatterie mit Dampfzufuhr aufgeschmolzen und eingespült werden. Eine Leitfähigkeitskontrolle der Waschlaugenkonzentration entfällt dabei.The type of flushing can also be carried out in various ways and adapted to the properties of the moldings or the existing washing technology. In the case of moldings with a low dissolution rate, the entire water supply is passed through the induction chamber and then the wash liquor is circulated through the chamber until the desired concentration is reached. This concentration can be determined and programmed using the electrical conductivity of the wash liquor. A similar procedure can be followed if large moldings intended for multiple washing processes are used. For moldings with a high dissolving speed, a partial flow can be branched off from the water inlet and passed through the induction chamber. The rate of dissolution can then also be influenced via the temperature of the water supplied. Molded portions portioned for a wash cycle or existing product residues can be melted and flushed in very quickly by adding hot water from a mixer tap with steam supply. A conductivity check of the wash liquor concentration is not necessary.
Ein von der Lösekammer abweichendes Konzept, das eine Reihe von Vorteilen bietet, ist eine Vorrichtung, die auf die Einspülkammer aufgesetzt oder darin integriert wird und den Waschmittelblock unter Bildung eines rieselfähigen Pulvers mechanisch zerkleinert. Der Zerreiber wird z. B. elektrisch angetrieben und trägt den Block schichtweise, z. B. mittels einer rotierenden oder vibrierenden Reibe ab. Die mechanische Dosierkammer hat in diesem Fall vorteilhaft ein Fassungsvermögen von mehreren vertikal gestapelten Formkörpern, die nacheinander den Zerkleinerungsbereich durchlaufen.Die Waschmitteldosierung kann über Leitfähigkeitskontrolle in der Waschflotte oder einfacher über die Ein schaltdauer des Zerreibers gesteuert werden. Zugleich mit dem Starten des Mahlgeräts spült ein Wasserstrahl das Pulver aus der Einspülkammer in die Waschmaschine.A concept deviating from the dissolving chamber, which offers a number of advantages, is a device which is placed on the induction chamber or integrated therein and mechanically comminutes the detergent block to form a free-flowing powder. The grinder is e.g. B. electrically driven and supports the block in layers, e.g. B. by means of a rotating or vibrating grater. In this case, the mechanical dosing chamber advantageously has a capacity of several vertically stacked moldings which pass through the shredding area one after the other. The detergent dosing can be carried out via conductivity control in the washing liquor or, more simply, via the one switching duration of the grater can be controlled. At the same time the grinder is started, a water jet rinses the powder from the dispenser into the washing machine.
Die in den Tabellen angegebenen schmelzbaren Rezepturbestandteile C und D wurden in einem beheizbaren Kneter zusammengeführt und bei Temperaturen zwischen 80 und 100 °C aufgeschmolzen. Anschließend wurden die festen Bestandteile, die eine Korngröße von 0,05 bis 0,5 mm aufwiesen, zugefügt und die Schmelze homogenisiert. Im Falle eines Zusatzes von Natriumperborat wurde die Schmelze zuvor auf 80 °C abgekühlt. Nach vollständiger Homogenisierung wurde die geschmolzene Masse in zylindrische Formen gegossen und rasch auf Raumtemperatur abgekühlt. Analytische Nachprüfungen ergaben, daß während des Abkühlens in der Gußform kein Entmischen bzw. Absetzen einzelner Kornfraktionen stattgefunden hatte.The meltable formulation components C and D given in the tables were combined in a heatable kneader and melted at temperatures between 80 and 100.degree. The solid constituents, which had a particle size of 0.05 to 0.5 mm, were then added and the melt was homogenized. If sodium perborate was added, the melt was previously cooled to 80 ° C. After complete homogenization, the molten mass was poured into cylindrical molds and quickly cooled to room temperature. Analytical tests showed that no separation or settling of individual grain fractions had taken place in the casting mold during cooling.
In der Tabelle bedeuten:
Claims (10)
10.Verfahren for dosing the agent according to one or more of the claims that the in a separate pantry housed in a shaped by means of a program-controlled, mechanically driven device in a quantity required for the respective washing process and the crushed portion in the wash liquor brings in.
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP89107370A EP0340589B1 (en) | 1988-05-02 | 1989-04-24 | Detergents in the form of fusible shaped bodies |
AT89107370T ATE91302T1 (en) | 1988-05-02 | 1989-04-24 | DETERGENT IN THE FORM OF MELTABLE MOLDED BODIES. |
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE3814857 | 1988-05-02 | ||
DE3814857A DE3814857A1 (en) | 1988-05-02 | 1988-05-02 | DETERGENT IN FORM OF MELTABLE FORMKOERPER |
EP89107370A EP0340589B1 (en) | 1988-05-02 | 1989-04-24 | Detergents in the form of fusible shaped bodies |
Publications (2)
Publication Number | Publication Date |
---|---|
EP0340589A1 true EP0340589A1 (en) | 1989-11-08 |
EP0340589B1 EP0340589B1 (en) | 1993-07-07 |
Family
ID=25867643
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP89107370A Expired - Lifetime EP0340589B1 (en) | 1988-05-02 | 1989-04-24 | Detergents in the form of fusible shaped bodies |
Country Status (2)
Country | Link |
---|---|
EP (1) | EP0340589B1 (en) |
AT (1) | ATE91302T1 (en) |
Cited By (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1994007991A1 (en) * | 1992-10-07 | 1994-04-14 | Henkel Kommanditgesellschaft Auf Aktien | Machine care stick |
WO1996003490A1 (en) * | 1994-07-22 | 1996-02-08 | Monsanto Company | Block detergent containing nitrilotriacetic acid |
WO1996003489A1 (en) * | 1994-07-22 | 1996-02-08 | Monsanto Company | Block detergent containing nitrilotriacetic acid |
WO2000058436A1 (en) * | 1999-03-29 | 2000-10-05 | Ecolab Inc. | Solid pot and pan detergent |
DE19924368A1 (en) * | 1999-05-27 | 2000-11-30 | Henkel Ecolab Gmbh & Co Ohg | Cleaning tablets containing surfactants |
DE19937428A1 (en) * | 1999-08-07 | 2001-02-08 | Henkel Kgaa | Detergent tablets |
DE10010760A1 (en) * | 2000-03-04 | 2001-09-20 | Henkel Kgaa | Laundry and other detergent tablets containing enzymes, e.g. controlled release tablets, have two or more uncompressed parts containing active substances and packaging system with specified water vapor permeability |
GB2367830A (en) * | 2000-10-12 | 2002-04-17 | Procter & Gamble | Process for preparing tablets |
WO2008000560A1 (en) * | 2006-06-27 | 2008-01-03 | Henkel Ag & Co. Kgaa | Detergent or treatment agent portion i |
WO2009021784A1 (en) * | 2007-08-14 | 2009-02-19 | Unilever N.V. | Detergent tablet |
EP0781320B2 (en) † | 1994-09-13 | 2013-10-16 | Kao Corporation | Washing method |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE1617093A1 (en) * | 1963-11-26 | 1971-02-25 | Fmc Corp | Process for the manufacture of detergent tablets |
EP0266200A2 (en) * | 1986-10-31 | 1988-05-04 | Unilever Plc | Detergent composition |
-
1989
- 1989-04-24 AT AT89107370T patent/ATE91302T1/en not_active IP Right Cessation
- 1989-04-24 EP EP89107370A patent/EP0340589B1/en not_active Expired - Lifetime
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE1617093A1 (en) * | 1963-11-26 | 1971-02-25 | Fmc Corp | Process for the manufacture of detergent tablets |
EP0266200A2 (en) * | 1986-10-31 | 1988-05-04 | Unilever Plc | Detergent composition |
Cited By (14)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1994007991A1 (en) * | 1992-10-07 | 1994-04-14 | Henkel Kommanditgesellschaft Auf Aktien | Machine care stick |
WO1996003490A1 (en) * | 1994-07-22 | 1996-02-08 | Monsanto Company | Block detergent containing nitrilotriacetic acid |
WO1996003489A1 (en) * | 1994-07-22 | 1996-02-08 | Monsanto Company | Block detergent containing nitrilotriacetic acid |
EP0781320B2 (en) † | 1994-09-13 | 2013-10-16 | Kao Corporation | Washing method |
US6608023B2 (en) | 1999-03-29 | 2003-08-19 | Ecolab Inc. | Solid pot and pan detergent |
US6387870B1 (en) | 1999-03-29 | 2002-05-14 | Ecolab Inc. | Solid pot and pan detergent |
WO2000058436A1 (en) * | 1999-03-29 | 2000-10-05 | Ecolab Inc. | Solid pot and pan detergent |
DE19924368A1 (en) * | 1999-05-27 | 2000-11-30 | Henkel Ecolab Gmbh & Co Ohg | Cleaning tablets containing surfactants |
DE19937428A1 (en) * | 1999-08-07 | 2001-02-08 | Henkel Kgaa | Detergent tablets |
DE10010760A1 (en) * | 2000-03-04 | 2001-09-20 | Henkel Kgaa | Laundry and other detergent tablets containing enzymes, e.g. controlled release tablets, have two or more uncompressed parts containing active substances and packaging system with specified water vapor permeability |
US7300911B2 (en) | 2000-03-04 | 2007-11-27 | Henkel Kommanditgesellschaft Auf Aktien | Method of preparing multiphase laundry detergent and cleaning product shaped bodies having noncompressed parts |
GB2367830A (en) * | 2000-10-12 | 2002-04-17 | Procter & Gamble | Process for preparing tablets |
WO2008000560A1 (en) * | 2006-06-27 | 2008-01-03 | Henkel Ag & Co. Kgaa | Detergent or treatment agent portion i |
WO2009021784A1 (en) * | 2007-08-14 | 2009-02-19 | Unilever N.V. | Detergent tablet |
Also Published As
Publication number | Publication date |
---|---|
EP0340589B1 (en) | 1993-07-07 |
ATE91302T1 (en) | 1993-07-15 |
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