WO1993016165A1 - Staubarme aniontensidkonzentrate in pulver- beziehungsweise granulatform mit verbessertem auflösevermögen - Google Patents
Staubarme aniontensidkonzentrate in pulver- beziehungsweise granulatform mit verbessertem auflösevermögen Download PDFInfo
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- WO1993016165A1 WO1993016165A1 PCT/EP1993/000302 EP9300302W WO9316165A1 WO 1993016165 A1 WO1993016165 A1 WO 1993016165A1 EP 9300302 W EP9300302 W EP 9300302W WO 9316165 A1 WO9316165 A1 WO 9316165A1
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- water
- anionic surfactant
- salts
- drying
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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
- C11D11/00—Special methods for preparing compositions containing mixtures of detergents ; Methods for using cleaning compositions
- C11D11/02—Preparation in the form of powder by spray drying
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D1/00—Evaporating
- B01D1/16—Evaporating by spraying
- B01D1/18—Evaporating by spraying to obtain dry solids
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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
- C11D11/00—Special methods for preparing compositions containing mixtures of detergents ; Methods for using cleaning compositions
- C11D11/0082—Special methods for preparing compositions containing mixtures of detergents ; Methods for using cleaning compositions one or more of the detergent ingredients being in a liquefied state, e.g. slurry, paste or melt, and the process resulting in solid detergent particles such as granules, powders or beads
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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
- C11D11/00—Special methods for preparing compositions containing mixtures of detergents ; Methods for using cleaning compositions
- C11D11/04—Special methods for preparing compositions containing mixtures of detergents ; Methods for using cleaning compositions by chemical means, e.g. by sulfonating in the presence of other compounding ingredients followed by neutralising
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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
- C11D17/06—Powder; Flakes; Free-flowing mixtures; Sheets
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B21/00—Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects
- F26B21/02—Circulating air or gases in closed cycles, e.g. wholly within the drying enclosure
- F26B21/04—Circulating air or gases in closed cycles, e.g. wholly within the drying enclosure partly outside the drying enclosure
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B3/00—Drying solid materials or objects by processes involving the application of heat
- F26B3/02—Drying solid materials or objects by processes involving the application of heat by convection, i.e. heat being conveyed from a heat source to the materials or objects to be dried by a gas or vapour, e.g. air
- F26B3/10—Drying solid materials or objects by processes involving the application of heat by convection, i.e. heat being conveyed from a heat source to the materials or objects to be dried by a gas or vapour, e.g. air the gas or vapour carrying the materials or objects to be dried with it
- F26B3/12—Drying solid materials or objects by processes involving the application of heat by convection, i.e. heat being conveyed from a heat source to the materials or objects to be dried by a gas or vapour, e.g. air the gas or vapour carrying the materials or objects to be dried with it in the form of a spray, i.e. sprayed or dispersed emulsions or suspensions
Definitions
- the invention relates to a new form of supply of washing and / or cleaning active anionic surfactant concentrates in the form of dust-free, solid, free-flowing powders and / or granules.
- the invention has the object of making washing and / or cleaning-active anionic surfactant compounds available in a form of supply which have not previously been available in this type in the combination of the substance properties.
- the invention aims in particular to provide fine particulate powders and / or granules with an arbitrarily adjustable anionic surfactant content - which should practically extend to the pure surfactant or surfactant mixture - which are characterized by low or no dust, high and adjustable bulk densities, which can be well over 150 g / l and at the same time have an optimized solution behavior in aqueous washing and / or cleaning liquors.
- the invention intends to provide such anionic surfactants and / or anionic surfactant mixtures which are characterized by practically any availability in terms of quantity, can be at a low level of the production price, optimally meet today's high-quality requirements for ecologically compatible surfactants or surfactant components and are therefore particularly suitable for making a significant contribution to the exchange of anionic surfactants based on alkylbenzenesulfonates which is sought today.
- the task according to the invention is based on making known anionic surfactants from starting materials of plant and / or animal origin available as essential components of the new non-dusting anionic surfactant concentrates.
- the invention is not restricted to these starting materials of plant and / or animal origin.
- Surfactant compounds of synthetic origin in particular ecologically compatible compounds of synthetic origin, are also preferred main and / or mixture components in the sense of the action according to the invention.
- Typical examples are the class of the half esters of sulfuric acid with fatty alcohols, especially long-chain saturated fatty alcohols, which play an important role under the term fatty alcohol sulfates (FAS), which derive from this dissipative fatty alcohol ether sulfates (FAES), which can be produced by alkoxylation, in particular ethoxylation and / or propoxylation, of fatty alcohols and subsequent sulfation of the alcohol components thus formed.
- FAS fatty alcohol sulfates
- FAES dissipative fatty alcohol ether sulfates
- anionic surfactants customary today fall into the class of the sulfonated fatty acids or their wash-active salts and the associated sulfonated fatty acid esters.
- Known surfactants from the last-mentioned class of substances are the alpha-sulfofatty acid methyl esters or their salts (MES) and the alpha-sulfonated carboxylic acids or their wash-active salts derived therefrom by ester cleavage and / or direct alpha-sulfonation of fatty acids, or their washing-active salts Di-salts "have become known.
- anionic surfactant compounds listed here only by way of example contain longer-chain organic residues, for example in the range from Cg_24 »in particular Ci2_i8 and are known mixture components in detergents and cleaning agents in which they are usually combined with other surfactants, in particular nonionic surfactant character, with orga ⁇ African and / or inorganic framework or builder substances as well as other conventional mixture components can be used.
- anionic surfactants for the wide replaceability of, for example, vegetable and / or animal-based anionic surfactants based on sulfate and / or sulfonate, the form of supply as dust-free pourable and free-flowing fine powder or granules would also be included high resolution speed is the ideal solution.
- Aqueous pastes as are often obtained as primary reaction products in the production of the anionic-surfactant compounds concerned here, pose a variety of problems for technical processing, both from considerations of stability and of handling of this form of supply.
- Alkyl sulfate pastes are on the one hand endangered by hydrolysis, and on the other hand all anionic surfactant pastes show strong viscosity fluctuations depending on the solids content of the respective aqueous paste up to the impossibility of transporting the aqueous pastes by pumps and lines and thus metering them, for example.
- anionic surfactants of the type concerned according to the invention into solids.
- compounds are proposed here which contain the anionic surfactants in admixture with dispersants, solubilizers and / or simply water-soluble salts. It is necessary to use these auxiliaries in connection with the production of dry supply forms according to the prior art, because the previous drying technology leads to limited use of anionic surfactant products by hot drying in spray towers and / or in the fluidized bed. Difficulties lie in particular in the following: The poor solubility and tendency towards gelling of important surfactant components also leads to dry powders which have a comparatively delayed solubility even when they are converted into a finely particulate dry state.
- anionic surfactant compounds of the type described can only be worked up into powder products of low bulk density by the drying technology known per se in hot air or in hot fuel gases in the spray tower technology customary today.
- auxiliaries for example inorganic salts as weighting agents, also only leads to a limited increase in the adjustable bulk densities of the dry surfactant powder.
- the bulk densities are often below 100 g / l.
- bulk densities of at most about 130 g / l can be set. Di-salts of the type described above cannot even be produced with such bulk densities, even after washing with auxiliary substances as dry powder.
- the bulk density that can be achieved on an industrial scale is generally well below 100 g / l.
- the present invention relates to the anionic surfactant concentrates described below in the form of solid, free-flowing powders and / or granules, which are also present as compounds in a mixture with other auxiliaries and / or valuable substances suitable for use in detergents and / or cleaning agents can and have been prepared by drying appropriate water-containing preparations with the formation of the powder and / or granule form.
- these anionic surfactant concentrates are now characterized in a first embodiment in that they contain the anionic surfactant compounds at least in part in the form of their washing and / or cleaning salts, having bulk densities of at least about 150 g / l and by hot drying the water-containing preparations with superheated steam as drying gas.
- Preferred bulk densities of these anionic surfactant concentrates are at or above about 200 g / 1, preferably at or above about 300 g / 1 and in particular at least about 350 g / 1.
- the anionic surfactant concentrates according to the invention are further characterized in particular by the fact that they are at least low in dust, in the preferred embodiment they are practically completely dust-free.
- they can be characterized in that they are dust-binding as mixture components in order to adjust these material properties - even the finest particles Contain auxiliaries and / or recyclables.
- the absence of dust can also be provided by regulating the residual water content in the pourable and free-flowing material.
- the invention relates to anionic surfactant concentrates in the form of a pourable granular material - hereinafter also referred to as "carrier bead" - which is characterized by an absorbent porous inner structure of the granular carrier beads.
- the invention relates to the process for the preparation of the anionic surfactant concentrates with the desired combination of material properties, as described above.
- the invention relates to the use of these anionic surfactant concentrates in dry form in particular aqueous washing and / or cleaning agents, in particular for at least partial exchange for anionic surfactants based on ABS.
- anionic surfactant materials can be produced in the finest powder form by spray drying.
- the resulting powders are just as dust-free as the old technology, which is the only way out prestigious surfactant granules, the production of which from previously obtained powders required an additional step using old technology.
- the anionic surfactant powders defined according to the invention are at the same time characterized by high bulk densities, which make handling, packaging and transporting this form of supply meaningful and economically portable.
- the high bulk densities which can be set, in the sense of the production of dry forms for detergents and cleaning agents which are desired today, are important as so-called heavy powders for immediately usable mixture components.
- such a form of supplying the anionic surfactant solids should then be associated with the disadvantage of a difficult or at least delayed dissolvability in aqueous liquors. According to the invention, this disadvantage no longer exists or is alleviated at least to such an extent that there are no longer any restrictions for the practical handling and utilization of the anionic surfactant concentrates defined according to the invention.
- the anionic surfactant concentrate defined according to the invention in detergent or cleaning surfactants is at least about 20% by weight and preferably at least about 30% by weight, based in each case on fine particles Solids.
- the surfactant solid as such can form the powder or granule grain.
- surfactant granules are particularly preferred according to the invention, whose active content of anionic surfactants is in the range from about 35 to 95% by weight.
- the temperature profile in the droplets of material to be dried differs from conventional drying methods by means of hot air and / or hot combustion gases when superheated steam is used as the drying medium as follows: when the material to be dried is brought into the atmosphere of the superheated at temperatures below 100 ° C. Steam condenses spontaneously heating the aqueous drop to the boiling point of the water under working conditions by condensing the superheated steam on the cooler feed material and releasing the heat of condensation to the material to be dried. When working under normal pressure, this means heating the temperature of the material to around 100 ° C. This boiling temperature is maintained as the minimum temperature in the drop of material during the entire drying period.
- auxiliaries which are solid in the temperature range of 100 ° C. and thus ensure the storage-stable pourability and free-flowing properties of the granular material dried in this way can be expedient or necessary.
- these auxiliary substances can in turn be selected valuable substances for the intended use or inert substances. You can build on the basis of organic and / or inorganic mixture components and thereby be water soluble and / or water insoluble.
- the result known from conventional spray drying can also be ensured when using superheated steam as the drying gas, the flowable wet insert material in fine particle form without any appreciable sticking of the particles to one another or at least under a controllable unit drying the position of the particle size.
- the anionic surfactant components present in these solids can be certain individual valuable substances of the type mentioned, but there can also be practically any desired mixtures of valuable substances of the surfactant class mentioned here.
- the term "surfactant mixture” is to be understood in several ways: Even within a selected class - for example fatty alcohol sulfates and / or fatty acid sulfonates - there is generally no individualized substance in the sense of a selected compound.
- surfactant mixtures in particular also includes, in the sense of the definition according to the invention, the targeted combination of anionic surfactants with fundamentally different structures.
- anionic surfactant dispersants which may be based, for example, on relatively shorter-chain sulfates and / or sulfonates.
- anionic surfactants are mixtures of, on the one hand, di-salts - ie alpha-sulfofatty acid salts, for example the chain length of C.sub.20-20, and on the other hand anionic surfactants based on fatty alcohol sulfates, for example based on TAS and / or based on alkyl ester sulfonates, in particular methyl ester sulfonates (MES).
- fatty alcohol sulfates for example based on TAS and / or based on alkyl ester sulfonates, in particular methyl ester sulfonates (MES).
- MES methyl ester sulfonates
- the invention provides in particular two proposed solutions which can also be used in combination with one another.
- One approach is based on the proposal to make targeted use of the residual water content of the goods to be dried. Depending on the nature of the solid material present in the individual case, control of the residual water in the dry material can at least largely make it dust-free.
- residual water contents are in the range from about 1 to 20% by weight, preferably at most about 10% by weight and in particular below 5 up to 7% by weight. Residual water contents in the range of up to 3 or 4% by weight can be particularly suitable, with values in the range of about 1 to 3% by weight generally providing satisfactory results. As the examples show, residual moisture values below 1% by weight can also be set.
- the teaching of the invention provides that the anionic surfactant concentrates may contain additional components in varying amounts, which in the embodiment discussed here serve primarily to remove dust formation or are to be regarded as dust-binding aids.
- the invention expressly includes the incorporation of such auxiliaries, which in turn represent valuable substances in the sense of use in detergents and / or cleaning agents or the joint use with the anionic surfactant components concerned in each case.
- the finely particulate pourable and free-flowing anionic surfactant concentrates of the invention are characterized in that, as dust-binding auxiliaries and / or valuable substances, they contain mixture components in a preferably homogeneous mixture which are liquid at room temperature - optionally in the presence of limited amounts of residual water and / or at least have a sticky nature and are preferably incorporated into the surfactant concentrate in such amounts that the required freedom from dust is ensured without lasting impairment of the pourability and free-flowing properties.
- Suitable dust-binding auxiliaries can be, in particular at room temperature, water-soluble, water-emulsifiable and / or water-swellable mixture components, which in turn are mono-compounds, oligomer compounds and / or suitably selected polymer compounds.
- inventive teaching here zugrundelie ⁇ constricting working concept is explained: The excipients can be due to their water solubility or Wassere ulgier stresses, 'but in any case also homogeneous due to their water swellability Work into the anionic surfactant mixture to be dried.
- the water-containing feedstock is then divided up particulate and in particular finely particulate in the superheated steam stream and dried under the action of superheated steam reliable and uniform mixing of these dust-binding aids in every particle in an even distribution.
- the dust-binding effect of this additive comes to the fore in the finally dried particle.
- Suitable water-soluble and flowable components under normal conditions are polyfunctional low-volatility alcohols or their oligomers, glycerol or corresponding oligoglycerols being of particular importance here for reasons of cost.
- Further examples of corresponding free-flowing compounds and / or compounds which at least impart sufficient tack under the action of residual water are mixture components such as oligomers and / or polymers of ethylene glycol and / or propylene glycol.
- polyethylene glycols - for example with a molecular weight range of up to approximately 10,000, preferably up to approximately 7,000, but in particular also corresponding oligo compounds with upper molecular weight limits of approximately 500 to 1,000, can be valuable substances in the sense of the action according to the invention which, like the representatives mentioned above, glycerol and / or oligoglycerols - not only bring about the desired dust binding, but are also solubilizers and / or valuable substances in the context of detergents and cleaners.
- auxiliaries are also mono- and / or oligoglycosides, examples of which are glucose, oligoglucoses, sugars such as succrose, sucrose or correspondingly higher ring numbers of sugars or sugar compounds, all the way to speaking polymer compounds of the type of starch and / or partially degraded starch and starch derivatives.
- all compounds of this type are distinguished, in particular in the presence of small amounts of water, by a more or less pronounced tackiness.
- these components which are present in low concentrations are taken up directly by the aqueous washing liquors and do not interfere with the desired washing or cleaning processes.
- glycoside compounds of the type in question are generally sufficiently hygroscopic as solids, despite their substitution with hydrocarbon residues which are active in washing or cleaning, for example C8-0- ⁇ ns ⁇ , special CIQ-18 SO , and which they have when mixed homogeneously into the anionic surfactants and in the drying of corresponding aqueous slurries can additionally take on the function of reliably binding powdery constituents.
- hydrocarbon residues which are active in washing or cleaning
- C8-0- ⁇ ns ⁇ special CIQ-18 SO
- Suitable mixture components for the reliable removal of the dust problem are, however, also oligomeric and / or polymeric mixture components, which in turn are preferably at least water-swellable and / or water-soluble.
- oligomeric and / or polymeric mixture components which in turn are preferably at least water-swellable and / or water-soluble.
- PVP polyvinylpyrrolidone
- PVA polyvinyl alcohol
- polycarboxylate compounds in particular of synthetic origin, which can be obtained, for example, by polymerization or copolymerization of (meth) acrylic acid and maleic acid or maleic anhydride and as a so-called builder component nent play a significant role in today's laundry detergents.
- oligo- or polyglycoses containing carboxyl groups are oligo- or polyglycoses containing carboxyl groups, as can be obtained by targeted oxidation of starch by introducing the carboxyl group in the 6-position on the glucose ring.
- Corresponding water-soluble and / or water-swellable cellulose derivatives such as methyl cellulose, carboxymethyl cellulose, hydroxyalkyl celluloses, such as hydroxyethyl cellulose and the like, are also suitable.
- nonionic surfactant components which are flowable or sufficiently tacky under normal temperature conditions can also be used as mixture components
- nonionic surfactant components which are flowable or sufficiently tacky under normal temperature conditions can also be used as mixture components
- Suitable anionic surfactant compounds are washing and / or cleaning active representatives of this class of substances in a wide range, as are available to the professional world today.
- natural substance-based materials are just as suitable as corresponding secondary products of synthetic chemistry.
- Preferred anionic surfactants are distinguished by increased ecological compatibility and are particularly suitable for the partial and / or complete replacement of the anionic surfactant based on ABS.
- anionic surfactant compounds for teaching the invention are fatty alcohol sulfates (saturated and / or unsaturated), fatty alcohol ether sulfates, olefin and / or alkane sulfonates, Fatty acid ester sulfonates, sulfated fatty acid triglycerides and / or glycerin fatty acid partial ester sulfates.
- anionic surfactants in the sense of the action according to the invention are succinic acid half-ester sulfonates which have a sufficiently oleophilic residue in their ester grouping - for example a fatty alcohol residue with 6 to 20 C atoms, in particular 10 to 16 C atoms point.
- fatty acid ester sulfonates are the known anionic surfactants based on alpha-sulfofatty acid lower alkyl esters or their salts, the most important representatives here again being the alpha-sulfofatty acid methyl esters (MES).
- MES alpha-sulfofatty acid methyl esters
- Typical representatives of fatty acid sulfonates are alpha-sulfo fatty acids or their washing- or cleaning-active salts, which are known in the art as "di-salts" and are accessible from free fatty acids and / or from corresponding alpha-sulfo fatty acid esters by ester cleavage.
- Sulfated fatty acid triglycerides are known to be reaction products of natural fats and / or oils with in particular SO3, which are obtained as multicomponent mixtures of active ingredients from sulfates and sulfonates and are described, for example, in the applications for property rights by applicant DE-A 3936001 and 3941 365.
- the washing and / or cleaning-active anionic surfactants are usually in the form of their alkali and / or ammonium salts or as soluble salts of organic bases.
- particularly important alkali salts are the sodium salts and the corresponding potassium salts.
- Any auxiliary substances used are usually present in amounts of at least 2 to 3% by weight, preferably in amounts of at least 5 to 10% by weight, based in each case on the multicomponent mixture.
- the teaching of the invention encompasses the mixing of the anionic surfactant compounds and their mixing with the mixture components listed above, in particular of an organic nature, also in Mixing with inorganic components.
- These can preferably be corresponding components from the field of common constituents of detergents and / or cleaning agents, which are advantageously also homogeneously incorporated into the powders and / or granules.
- water-soluble inorganic mixture components are water-soluble salts such as sodium carbonate, sodium bicarbonate and / or sodium sulfate, but also water-soluble sodium silicates, in particular the water glasses typical of detergents and cleaning agents.
- water-insoluble mixture components can be incorporated into the powdery anionic surfactant agglomerates.
- An example is given here: Synthetic zeolite compounds, in particular zeolite NaA in detergent quality and a calcium binding capacity in the range from 100 to 200 mg CaO / g - compare the details in DE 24 12837.
- anionic surfactant concentrates designed according to the invention is just becoming clear from the use of such insoluble inorganic constituents it can be seen: if, for example, tallow alcohol sulfate (TAS) is subjected to a conventional spray-drying process together with zeolite NaA, the detergent-active TAS component is applied to the zeolite particles in such a tightly closed layer that in the subsequent use, substantial portions of the washing power can no longer be formed in the aqueous liquor.
- TAS tallow alcohol sulfate
- this negative effect when zeolite is added does not exist, or at least to a very greatly reduced extent.
- water-insoluble possible mixed components are finely divided swellable layered silicates of the type of corresponding montmorillonites, for example bentonite.
- the general rule specified in DE-A 4030688, already mentioned several times also applies to the valuable substances and auxiliary substances to be used in the context of the present invention, according to which such valuable substances or Combinations of valuable materials and auxiliary materials are suitable which are not or not significantly damaged by short-term exposure to water or water vapor in the temperature range from 100 to 110 ° C.
- Components of this type which, under the working conditions, have the specified temperature range at least for a period of about 0.5 to 1 min are particularly suitable as components of valuable materials. Survive harmless.
- surfactant compounds per se which are susceptible to hydrolysis can survive dwell periods of a few minutes largely undamaged under these working conditions if certain general conditions known to the relevant expert are observed. It is thus possible in the process according to the invention to work up aqueous preparations of anionic surfactants such as FAS and / or MES which are inherently susceptible to hydrolysis to dust-free dry powders.
- corresponding active substance preparations are thus also in particular which are designed as a porous carrier bead for the production of solid wetting agents, detergents and / or cleaning agents and are characterized in that they are absorbent porous Have internal structure, at least about 35 wt .-% wt .-% based on porous carrier bead - consist of anionic surfactants and have been produced by spray and / or fluidized bed drying in superheated steam.
- porous carrier beads containing anionic surfactants in high concentration are suitable for direct use in wetting agents, detergents and / or cleaning agents, or else initially for loading the basic grain with valuable substances from the subject area mentioned, for example, further surfactant components. Details of this are the subject of the disclosure of the aforementioned German patent application P 42 34 376.3 of the applicant.
- a particularly important embodiment of the carrier beads according to the invention with a microporous inner structure in corresponding embodiments with anionic surfactant contents of the unloaded carrier bead is at least about 50% by weight, the anionic surfactant content being up to 70, 80 or even up to 90 can be up to 95% by weight of the carrier bead.
- the carrier bead can be formed almost entirely from the surfactant component.
- the dried carrier bead is present as a solid in the temperature range from approximately 100 to 110 ° C. and preferably in the temperature range to approximately 120 ° C., the plasticity and surface tack of which are obtained by suitable selection and combination of the components forming the carrier bead are restricted in such a way that substantial bonding of the particles to one another and / or substantial bonding of their open-pore internal structure are eliminated even under the conditions of exposure to the superheated steam.
- the teaching according to the invention thus ensures that the special, highly porous structural structure of the material to be dried, which primarily occurs during drying with superheated steam, is fixed in such a way that it is in the inevitable mechanical pressure and contact stresses for such a granular material even in the range of elevated temperatures and optionally maintained in the presence of superheated steam.
- surfactant component in the carrier bead the higher the content of surfactant component in the carrier bead, the more the individual properties of the surfactant used come to the fore in the behavior of the porous carrier bead.
- these anionic surfactant concentrates contain mixtures with water-soluble and / or finely divided water-insoluble inorganic and / or organic auxiliaries and / or valuable substances, the selection of which is made in such a way that the restrictions according to the invention of plasticity and / or the surface stickiness in the temperature range around 100 to 120 ° C are guaranteed.
- such mixture components are present in minor amounts, based on the anionic surfactants in the carrier bead.
- this is the first time that solid dry valuable substance preparations in the field of wetting agents, detergents and cleaning agents have been obtained, in which a solid carrier bead is at least predominantly based on anionic surfactant.
- the previous detergent technology does not know such substance preparations.
- the temperature behavior of the components forming the carrier bead and in particular of the surfactant components used here in the preferred embodiment according to the invention in the temperature range from about 100 to 120 ° C. has a decisive influence on the composition of the valuable and auxiliary substances for the carrier bead structure to be selected in each case.
- Important anionic surfactants for example fatty alcohol sulfates (FAS) of long-chain fatty alcohols, a large number of wash-active sulfates, but also nonionic surfactant compounds, for example alkylglycoside compounds of long-chain fatty alcohols, are in the Although the temperature range mentioned is still stable in the solid phase, its plasticity and, in particular, surface stickiness may have increased comparatively strongly.
- the invention provides that the thermally unsatisfactory constituents for the carrier bead can be used fully by using mixture components which ensure the required temperature stability and in particular the required low values in surface tack and plasticity .
- mixture components can be valuable substances in the sense of detergent and cleaning agent mixtures customary today, but auxiliaries can also be used which do not develop their own function in the intended field of application, but which do not interfere with the use of the valuable substances or combinations of valuable substances prepared according to the invention .
- auxiliaries can be water-soluble and / or water-insoluble. They can be inorganic and / or organic in nature. In the case of the water-insoluble compounds, finely divided inorganic and / or organic auxiliaries are usually also used. The following information is only to be understood as an example:
- Suitable water-soluble inorganic auxiliaries for reducing the surface stickiness and plasticity of organic components are salts such as phosphates, in particular STP, sodium sulfate or sodium carbonate.
- salts such as phosphates, in particular STP, sodium sulfate or sodium carbonate.
- soluble sodium silicates of the type of water glasses and / or alkali hydroxide can also have a corresponding function.
- Insoluble inorganic mixture components for stabilizing the carrier bead consistency and reducing the surface stickiness are, for example, builder components based on zeolite, in particular zeolite NaA in detergent quality, and others Swellable or non-swellable layered silicates, for example corresponding montmorillonites such as bentonite and the like.
- other builder components based on solid, in particular crystalline, silicate compounds, which are known in today's detergent technology can also be considered here.
- salts of low molecular weight organic components in the sufficiently dried state are generally non-tacky components even at elevated temperatures.
- Suitable organic builders such as the alkali metal salts of polycarboxylic acids, for example citric acid, adipic acid, succinic acid, nitrilotriacetic acid and the like, are suitable here.
- Organic polymer substances such as are customary in detergents and cleaning agents, for example corresponding components based on cellulose derivatives and / or PVP, or else inert organic polymer, are also suitable as auxiliaries for stabilizing the carrier bead, even in the high temperature range materials such as cellulose powder and the like.
- the basic principle is that suitable substance mixtures and mixing ratios can be determined in a preliminary test using a working method which is familiar to the person skilled in the art. After appropriate preliminary tests have been carried out, the selected mixtures of substances can then be subjected to spray drying from aqueous preparations in superheated steam. The resulting granular dry matter shows in the subsequent treatment with a flowable phase whether and to what extent the desired fine-porous structure and thus the loadability of the carrier bead formed are also formed in its inner structure.
- di-salts which are known to be salts, preferably the alkali salts of wash-active alpha-sulfonated sulfo fatty acids.
- Di-salts or di-salt mixtures of technical purity can not only be worked up to the porous carrier bead without the addition of further auxiliary components, they can in turn be auxiliaries for thermally less stable anionic surfactant components such as FAS, FAES, MES, ABS and the like.
- the basic structure of the porous carrier bead is formed with the use of anionic surfactants from the classes of the carboxylates, the sulfonates including the ester sulfonates, the di-salts and / or the sulfates.
- anionic surfactant components for the construction of the carrier bead are alkylbenzenesulfonates (ABS), fatty alcohol sulfates (FAS), fatty alcohol ether sulfates (FAES), alpha-methyl ester sulfonates (MES) and / or di-salts.
- the carrier beads can be selected Contain anionic surfactants or mixtures of several anionic surfactants, which are generally constructed in a mixture with water-soluble and / or finely divided water-insoluble inorganic and / or organic auxiliaries and / or valuable substances without a surfactant character.
- the carrier beads contain the anionic surfactants in their grain structure in admixture with sufficiently temperature-stable other valuable substances in the field of wetting, washing and / or cleaning agents.
- suitable additives are in particular also those components which are capable of improving the anionic surfactant dissolution in aqueous phases. Examples of these are conventional dispersants, hydrotropes, structure breakers and the like.
- the teaching of the invention expressly also includes the porous and unloaded carrier beads which are designed in the manner described and contain valuable and possibly auxiliary substances in the specified field of application and at the same time improve water solubility.
- the porous and unloaded carrier beads which are designed in the manner described and contain valuable and possibly auxiliary substances in the specified field of application and at the same time improve water solubility.
- anionic surfactants such as FAS
- structure breakers which are often highly effective even in very small amounts, based on anionic surfactant, can be important are.
- a number of such dispersants or structure breakers in subgroups (a) to (g) are summarized below.
- a number of both solid and liquid substances which are hydrophilic, water-soluble or water-dispersible are suitable as structure breakers.
- Suitable are, for example, lower polyalkylene glycols which are derived from straight-chain or branched-chain glycols having 2 to 6 carbon atoms, preferably polyethylene glycol or polypropylene glycol, and have a relative molecular weight between 200 and 12,000.
- polyethylene glycols with a relative molecular weight between 200 and 4,000 are preferred, the liquid polyethylene glycols with a relative molecular weight up to 2,000 and in particular between 200 and 600 having particularly advantageous properties.
- the sulfates and in particular the disulfates of never their polyalkylene glycols, in particular polyethylene glycol and 1,2-propylene glycol, are also suitable. Particularly preferred are the sulfates and / or disulfates, which are derived from polyethylene glycols and polypropylene glycols with a relative molecular weight between 600 and 6,000 and in particular between 1,000 and 4,000.
- the disulfates generally originate from polyglycol ethers of the type which - caused by slight traces of water - can arise in the alkoxylation of alcoholic components.
- Another group of suitable structure breakers consists of the water-soluble salts of mono- and / or disulfosuccinates of the lower polyalkylene glycols.
- Suitable structure breakers consists of the water-soluble salts of mono- and / or disulfosuccinates of the lower polyalkylene glycols.
- any salts but preferably the alkali metal salts, in particular the sodium and potassium salts, and ammonium salts and / or salts of organic amines, for example triethanolamine, can be used as structure breakers for the use of the anionically modified polyalkylene glycols.
- the most important salts for practical use are the sodium salts of sulfates, disulfates, sulfosuccinates and disulfosuccinates of polyethylene glycol and polypropylene glycol.
- Mixtures of the polyalkylene glycols and their anionically modified derivatives are preferably also used in any mixing ratio.
- a mixture of polyalkylene glycol and the sulfosuccinates and / or disulfosuccinates of the polyalkylene glycols is preferred.
- a mixture of polyalkylene glycol and the corresponding sulfates and / or disulfates and a mixture of polyalkylene glycol and the corresponding sulfates and / or disulfates and the corresponding sulfosuccinates and / or sulfodisuccinates are also suitable.
- suitable and preferably used structure breakers are the addition products of about 20 to about 80 moles of ethylene oxide with 1 mole of an aliphatic alcohol with essentially 8 to 20 carbon atoms, the long-known ingredients of detergents and cleaning agents represent.
- the investment products from are particularly important 20 to 60 mol and in particular 25 to 45 mol ethylene oxide to primary alcohols, such as, for example, coconut oil alcohol or tallow fatty alcohol, to oleyl alcohol, to oxo alcohols, or to secondary alcohols having 8 to 18 and preferably 12 to 18 carbon atoms.
- Examples of particularly preferred structure breakers from the group of highly ethoxylated alcohols are taig fat alcohol with 30 E0 and taig fat alcohol with 40 E0. It is also preferred to use mixtures which contain highly ethoxylated alcohols, for example mixtures of tallow fatty alcohol with 40 E0 and water or of tallow fatty alcohol with 40 E0 and polyethylene glycol with a relative molecular weight between 200 and 2,000.
- Further suitable structure breakers are ethoxylated, vicinal internal alkanediols or 1,2-alkanediols with a carbon chain with 8 to 18 carbon atoms and 4 to 15 moles of ethylene oxide per mole of diol. It is possible for only one of the two OH groups or both OH groups of the alkanediol to be ethoxylated.
- Modified nonionic surfactants with a terminal acid group are also suitable as structure breakers. These are nonionic surfactants, in particular fatty alcohols, in which a 0H group has been converted into a group with a carboxyl group.
- Nonionic surfactants with a terminal acid group thus include esters or partial esters of a nonionic surfactant with a polycarboxylic acid or a polycarboxylic anhydride.
- acid-terminated nonionic surfactants are the known polyether carboxylic acids and esters or half esters of Cg-18 alcohols with succinic anhydride, maleic anhydride, maleic acid or citric acid.
- Another group of suitable structure breakers consists of alkylene glycol monoalkyl ethers of the general formula
- R 4 represents a radical with 2 to 6 carbon atoms and n represents a number from 1 to 8.
- examples of this group of additives are ethylene glycol monoethyl ether and diethylene glycol monobutyl ether.
- the working conditions of the method according to the invention enable the use of high temperatures of the water vapor phase which is circulated in the region of the drying step of the spray drying.
- the working temperatures of the feed steam are above 150 ° C. and preferably at least about 200 ° C. in the gas phase.
- Working temperatures of 250 ° C. and above can be of particular interest, the temperature range of at least 300 ° C., in particular 300-380 ° C., being particularly suitable.
- Working temperatures in the range of about 270 - 350 ° C in the water vapor phase are particularly suitable for many cases. All these temperature specifications relate in each case to the temperature of the water vapor flow heated to the spray zone in cocurrent or countercurrent and heated to the optimum temperature.
- Embodiments are possible here which contain only a limited reduction in the steam temperature after leaving the spray zone, for example to values in the range from approximately 190-250 ° C., while in other embodiments a further utilization of the thermal energy of the steam up to a reduction in the steam temperature is possible in the vicinity of the condensation temperature under process conditions - 100 to 110 ° C - can be expedient or advantageous.
- the closed system in principle, one works with a water vapor circuit stream from which the evaporated water portion of the feed material is extracted, while the amount of energy given off in particular in the drying step is fed back to the circuit stream in a direct or preferably indirect way.
- the water vapor stream which has been drawn off is supplied in an important embodiment as service steam after the cleaning of carried-along material portions, after the pressure and temperature of this steam stream have first been adjusted to the conditions required there, if desired.
- MARINE LEAF condensed steam component streams to cause, for example, wet washing of the withdrawn steam component stream and its cleaning of carried material portions.
- the resulting aqueous liquid phase can be returned to the drying process together with the recycled files present therein.
- the recirculated liquid components with valuable substance contents can be fed directly to the spray zone or first mixed with the aqueous fresh preparations and added to the spray zone in this form for drying.
- a particularly interesting embodiment of the teaching according to the invention provides for the recovery and utilization of the heat of condensation of the water vapor portion discharged from the circuit.
- the recycling of even small amounts of recyclable materials can be ensured, which have left the primary cycle of the steam via the discharged hot steam flow.
- the following can be used using the heat of condensation of the discharged steam:
- the steam condensate is concentrated using the heat of condensation of the partial steam stream drawn off.
- the remaining concentrate is returned to the primary process circuit.
- this residual concentrate can be added to the material slurry to be dried by superheated superheated steam.
- the method according to the invention enables for the first time the possibility of valuable substances and mixtures of valuable substances from the field of washing and cleaning agent exhaust air in the field of industrial production concerned here -to win free and free of loaded wastewater.
- the drying with the superheated steam can be carried out on the one hand as spray drying and / or on the other hand as drying in a fluidized bed.
- Comparatively high-water-containing materials are, for example, in the form of flowable and sprayable aqueous solutions, emulsions and / or suspensions of the materials or materials to be dried.
- feedstocks of this type are subjected to the spray drying technology known per se.
- Spray drying can be carried out in appropriately equipped spray towers in cocurrent or countercurrent mode. The use of the counter current principle is also preferred as part of the inventive work with superheated steam as the drying hot gas.
- the direct or preferably indirect energy input for supplying the evaporation energy into the steam circuit at least predominantly outside the drying zone.
- the result known from conventional spray drying the flowable wet one, is ensured Dry the feed material in fine particle form without appreciable sticking of the particles to one another or at least with a controllable setting of the particle size.
- the energy input to the steam circuit outside of the spray drying zone can be carried out in any known form of indirect heat transfer.
- An example is the use of tube bundle systems, which are flowed through by heating gases of any origin on the one hand and, on the other hand - but separately from these heating gases - by the steam flow to be heated.
- this indirect energy input into the steam cycle is carried out by means of one or more integrated burners with indirect heat transfer to the steam flow, the hot combustion gases being passed on the burner side directly into the heat exchanger which enters the steam cycle is integrated.
- the temperature of the combustion gases can be, for example, in the range from approximately 400 to 1,000 ° C. and in particular in the temperature range from approximately 650 to 960 ° C.
- at least 30% by volume and preferably more than 40% by volume of the hot flue gases can be recycled after leaving the integrated heat exchanger for further energy utilization.
- the amount of flue gas circulation is preferably more than 60% by volume and often in the range of about 70% by volume of the combustion gases supplied. All conventional fuel gases, in particular natural gas or comparable lower hydrocarbons or hydrocarbon mixtures and / or hydrogen, are suitable for operating the burner. If, on the other hand, the drying principle according to the invention is used in the context of fluidized-bed drying, the required heating of the drying gas based on steam can be brought about both outside the drying zone and with heat exchanger elements which are integrated in the fluidized bed. These two mechanisms of gas heating can also be connected to one another.
- Suitable working pressures are, for example, in the range up to about 0.15 bar, suitably up to about 0.075 bar and preferably below 0.05 bar. The range from about 0.005 to 0.015 bar system internal pressure can be particularly preferred.
- Drying with superheated steam in the sense of the teaching according to the invention is of course also possible in principle in the case of negative pressures, in particular in the area of moderate negative pressures, but then requires an increased technical outlay in order to ensure the exclusion of possible damage points in the circulatory system which would trigger undesirable air ingress.
- the numerical values given above apply mutatis mutandis to preferred negative pressure.
- Epton wash active substance 26.3%, based on slurry. Unsulfonated fatty acid 2.09%. Sodium sulfate 3.1%. Sodium chloride 2.2%. Degree of sulfation 89.6%.
- the product obtained had a dry matter content of 99.8% and a bulk density of 370 g / 1. It showed very favorable dissolving properties when added to water.
- Example 2
- Example 1 The procedure was as in Example 1. A slurry with a solids content of 36% was dried, which contained the above-mentioned sodium salt of a Ciö / Cig-alpha-sulfofatty acid (with admixtures) and polyethylene glycol with a molecular weight of 2000 in a weight ratio of the dry substances of 9: 1.
- the tower inlet temperature was 300 ° C; the outlet temperature at 210 ° C; all other parameters were comparable.
- the product had a dry matter content of 99% by weight; the bulk density was 290 g / 1.
- the aqueous slurry of fatty alcohol sulfate used is a white to pale yellow, solid paste with the following characteristics:
- the product obtained had a dry matter content of 99.2% by weight.
- the bulk weight was 293 g / 1.
- a 90% solubility in water at 20 ° C was achieved at 40 seconds.
- Example 3 An aqueous slurry with a solids content of 53.3% by weight, which was composed of the sodium salt of a / iQ fatty alcohol sulfate mentioned in Example 1 and a finely divided sodium aluminum silicate (zeolite NaA in detergent quality) in a 48% suspension, was dried on, which was stabilized with 1.5% by weight of tallow alcohol polyglycol ether.
- the mixture ratio (dry weight) of anionic surfactant to silicate was 2: 1.
- the dry product had a bulk density of 316 g / l and a solubility (90%) of 10 seconds.
- the procedure was as in Examples 3 and 4. A slurry with a solids content of 24.1% was dried in the superheated steam phase.
- the solids constituents of the starting mixture were the sodium salt of a cis / ig-fatty alcohol sulfate mentioned in Example 3, the disodium salt of a Ciö / iß-alpha-sulfofatty acid and sodium carbonate in a mixing ratio of 4: 1: 1.
- the dried carrier bead Powder had a bulk density of 220 g / l and a solubility (90%) of 20 seconds.
- Sulfopon T55 (trade name of the applicant): anionic surfactant based on Ciö / ig fatty alcohol sulfate
- Sulfopon K35 anionic surfactant
- Disalz Na disalz of a Ci5 / i8-alpha-sulfofatty acid mixture
- Texapon N70 Na lauryl ether sulfate, approx. 2E0
- Texin ES68 Ci / is- ⁇ -sulfofatty acid methyl ester
- Dehydol TA40 tallow alcohol ethoxylate (40 E0 on average)
- Water glass A Water-soluble sodium silicate in detergent quality
- APG Ci2 / i4 alkyl glucoside (DP approx.1.4)
- ABS wash-active alkylbenzenesulfonate (55% by weight aqueous paste)
- a slurry of the sodium salt of a Ci6 / 18-F et talc alcohol sulfate was added to a free-flowing surfactant powder with the addition of sodium carbonate and sucrose.
- the mixing ratio between the anionic surfactant, sodium carbonate and sucrose was 80: 17: 3, based on dry matter.
- the aqueous slurry of fatty alcohol sulfate used is a white to pale yellow solid paste with the following characteristics: Epton-containing substance: 54 - 58%
- A2S04 content ⁇ 2% pH (3% aqueous preparation): 10 - 11.5
- the slurries had a dry matter content of 47.7% by weight.
- the product obtained was a white, odorless powder with a dry matter content of 99.2% by weight.
- the bulk density was 310 g / l. It showed very good wettability and a favorable dissolving power when cold water was added.
- Example 7 An aqueous preparation of the above-mentioned Ciö / is fatty alcohol sulfate was dried, Sodium carbonate, sucrose and polyethylene glycol with an average molecular weight of 400. The mixing ratio was 80: 14: 3: 3 in terms of dry matter. The solids sodium carbonate and sucrose were dissolved in 3 parts of water and mixed into the slurry. The feed pump pressure was 4.3 to 4.6 bar and the amount of propellant gas in the two-fluid nozzle was 3.8 m 3 / h; all other parameters were comparable to the information in Example 7. The product had a dry matter content of 99.3% by weight. The bulk weight was 280 g / 1. The product is easily soluble in water.
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Abstract
Description
Claims
Priority Applications (6)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US08/290,860 US5536430A (en) | 1992-02-12 | 1993-02-09 | Process of producing low-dust anionic surfactant concentrates in powder or granule form with improved solubility in aqueous media |
EP93903932A EP0626005B1 (de) | 1992-02-12 | 1993-02-09 | Staubarme aniontensidkonzentrate in pulver- beziehungsweise granulatform mit verbessertem auflösevermögen |
DE59307819T DE59307819D1 (de) | 1992-02-12 | 1993-02-09 | Staubarme aniontensidkonzentrate in pulver- beziehungsweise granulatform mit verbessertem auflösevermögen |
JP5513776A JPH07503987A (ja) | 1992-02-12 | 1993-02-09 | 溶解性を改良した、ダストを含有しない粉末状または顆粒状のアニオン界面活性剤濃厚物 |
BR9305863A BR9305863A (pt) | 1992-02-12 | 1993-02-09 | Novo tipo de concentrados tensoativos anionicos pobres em poeira em forma de po ou de granulado com capacidade de dissolução melhorada em meios aquosos |
KR1019940702788A KR950700400A (ko) | 1992-02-12 | 1994-08-12 | 수성매질에서의 용해성이 향상된 분말 또는 과립형태의 저분진 음이온계 계면 활성제 농축물(new low-dust anionic surfactant concentrates in powder or granule form with improved solubility in aqueous media) |
Applications Claiming Priority (8)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DEP4204035.3 | 1992-02-12 | ||
DE4204035A DE4204035A1 (de) | 1992-02-12 | 1992-02-12 | Verbessertes verfahren zur trocknung von wertstoffen fuer wasch- und reinigungsmittel mit ueberhitztem wasserdampf |
DEP4204090.6 | 1992-02-12 | ||
DE19924204090 DE4204090A1 (de) | 1992-02-12 | 1992-02-12 | Vereinfachtes trocknungsverfahren fuer wertstoffe und wertstoffgemische aus dem bereich der wasch- und reinigungsmittel mit ueberhitztem wasserdampf |
DEP4206050.8 | 1992-02-27 | ||
DE19924206050 DE4206050A1 (de) | 1992-02-27 | 1992-02-27 | Neuartige staubarme aniontensidkonzentrate in pulver- beziehungsweise granulatform mit verbessertem aufloesevermoegen in waessrigen medien |
DE4234376A DE4234376A1 (de) | 1992-10-12 | 1992-10-12 | Wertstoffe und Wertstoffgemische für Netz-, Wasch- und/oder Reinigungsmittel in neuer Zubereitungsform |
DEP4234376.3 | 1992-10-12 |
Publications (1)
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WO1993016165A1 true WO1993016165A1 (de) | 1993-08-19 |
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ID=27435392
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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PCT/EP1993/000302 WO1993016165A1 (de) | 1992-02-12 | 1993-02-09 | Staubarme aniontensidkonzentrate in pulver- beziehungsweise granulatform mit verbessertem auflösevermögen |
Country Status (10)
Country | Link |
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US (1) | US5536430A (de) |
EP (1) | EP0626005B1 (de) |
JP (1) | JPH07503987A (de) |
AT (1) | ATE161038T1 (de) |
AU (1) | AU3496093A (de) |
BR (1) | BR9305863A (de) |
CA (1) | CA2130002A1 (de) |
DE (1) | DE59307819D1 (de) |
ES (1) | ES2110596T3 (de) |
WO (1) | WO1993016165A1 (de) |
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FR2751557A1 (fr) * | 1996-11-18 | 1998-01-30 | Niro France | Procede d'evaporation partielle d'un produit liquide et application de ce procede a la fabrication d'une poudre |
EP2406363B1 (de) | 2009-03-13 | 2018-12-12 | The Procter and Gamble Company | Sprühtrockungsverfahren |
WO2023229962A1 (en) * | 2022-05-24 | 2023-11-30 | Chemlink Laboratories, Llc | Process for removing water from a functional ingredient composition, and compositions containing the resulting product |
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US5637560A (en) * | 1992-02-12 | 1997-06-10 | Henkel Kommanditgesellschaft Auf Aktien | Process for the production of surface-active anionic surfactant salts using superheated steam |
IL108500A (en) * | 1994-01-31 | 1998-06-15 | Zohar Detergent Factory | Fatty alcohol sulphates in granular form and process for their preparation |
DE4406592A1 (de) * | 1994-03-01 | 1995-09-07 | Henkel Kgaa | Verbesserte Mehrstoffgemische auf Basis wasserlöslicher Alkalisilikatverbindungen und ihre Verwendung, insbesondere zum Einsatz als Builder in Wasch- und Reinigungsmitteln |
AU6298996A (en) * | 1995-06-26 | 1997-01-30 | Kruger A/S | A method and an apparatus for drying and combusting water-containing matter |
ES2167634T3 (es) * | 1996-04-09 | 2002-05-16 | Bayer Ag | Procedimiento y dispositivo para la aglomeracion de sustancias sensibles a la hidrolisis mediante vapor de agua. |
US6610752B1 (en) | 1999-10-09 | 2003-08-26 | Cognis Deutschland Gmbh | Defoamer granules and processes for producing the same |
DE19956803A1 (de) | 1999-11-25 | 2001-06-13 | Cognis Deutschland Gmbh | Tensidgranulate mit verbesserter Auflösegeschwindigkeit |
DE19962859A1 (de) * | 1999-12-24 | 2001-07-12 | Cognis Deutschland Gmbh | Feste Waschmittel |
DE19962886A1 (de) * | 1999-12-24 | 2001-07-05 | Cognis Deutschland Gmbh | Tensidgranulate mit verbesserter Auflösegeschwindigkeit |
DE10002009A1 (de) * | 2000-01-19 | 2001-07-26 | Cognis Deutschland Gmbh | Tensidgranulate |
DE10003124A1 (de) * | 2000-01-26 | 2001-08-09 | Cognis Deutschland Gmbh | Verfahren zur Herstellung von Tensidgranulaten |
DE10004678A1 (de) * | 2000-02-03 | 2001-08-09 | Cognis Deutschland Gmbh | Tensidgranulate |
DE10007322A1 (de) * | 2000-02-17 | 2001-08-23 | Cognis Deutschland Gmbh | Perlglanzmittel |
DE10012949A1 (de) * | 2000-03-16 | 2001-09-27 | Henkel Kgaa | Kieselsäureester-Mischungen |
DE10019344A1 (de) | 2000-04-18 | 2001-11-08 | Cognis Deutschland Gmbh | Wasch- und Reinigungsmittel |
DE10044471A1 (de) | 2000-09-08 | 2002-03-21 | Cognis Deutschland Gmbh | Waschmittel |
DE10044472A1 (de) | 2000-09-08 | 2002-03-21 | Cognis Deutschland Gmbh | Waschmittel |
GB2372518B (en) | 2001-02-21 | 2003-04-16 | Schlumberger Holdings | Powder composition |
DE10120263A1 (de) * | 2001-04-25 | 2002-10-31 | Cognis Deutschland Gmbh | Feste Tensidzusammensetzungen, deren Herstellung und Verwendung |
DE10163856A1 (de) * | 2001-12-22 | 2003-07-10 | Cognis Deutschland Gmbh | Hydroxymischether und Polymere in Form von festen Mitteln als Vorcompound für Wasch-, Spül- und Reinigungsmittel |
GB2399084B (en) * | 2002-07-30 | 2007-01-31 | Univ Liverpool | Porous beads and method of production thereof |
GB0228584D0 (en) * | 2002-12-07 | 2003-01-15 | Unilever Plc | Detergent compositions |
JP5247801B2 (ja) * | 2007-07-26 | 2013-07-24 | カーギル インコーポレイテッド | デンプンの変性方法 |
US20100300694A1 (en) * | 2007-11-20 | 2010-12-02 | Anja Vonderhagen | Method for producing an organic composition containing an n-nonyl ether |
EP2801605A1 (de) * | 2013-05-07 | 2014-11-12 | The Procter and Gamble Company | Sprühgetrocknetes Waschmittelpulver |
MY187405A (en) | 2014-09-29 | 2021-09-22 | Malaysian Palm Oil Board | Powder form of methyl ester sulphonates (mes) and process for producing the same |
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- 1993-02-09 EP EP93903932A patent/EP0626005B1/de not_active Expired - Lifetime
- 1993-02-09 DE DE59307819T patent/DE59307819D1/de not_active Expired - Fee Related
- 1993-02-09 BR BR9305863A patent/BR9305863A/pt not_active Application Discontinuation
- 1993-02-09 ES ES93903932T patent/ES2110596T3/es not_active Expired - Lifetime
- 1993-02-09 AT AT93903932T patent/ATE161038T1/de not_active IP Right Cessation
- 1993-02-09 US US08/290,860 patent/US5536430A/en not_active Expired - Fee Related
- 1993-02-09 CA CA002130002A patent/CA2130002A1/en not_active Abandoned
- 1993-02-09 WO PCT/EP1993/000302 patent/WO1993016165A1/de active IP Right Grant
- 1993-02-09 JP JP5513776A patent/JPH07503987A/ja active Pending
- 1993-02-09 AU AU34960/93A patent/AU3496093A/en not_active Abandoned
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---|---|---|---|---|
FR2751557A1 (fr) * | 1996-11-18 | 1998-01-30 | Niro France | Procede d'evaporation partielle d'un produit liquide et application de ce procede a la fabrication d'une poudre |
WO1998022194A1 (fr) * | 1996-11-18 | 1998-05-28 | Niro Kestner | Procede d'evaporation partielle d'un produit liquide et application de ce procede a la fabrication d'une poudre |
EP2406363B1 (de) | 2009-03-13 | 2018-12-12 | The Procter and Gamble Company | Sprühtrockungsverfahren |
WO2023229962A1 (en) * | 2022-05-24 | 2023-11-30 | Chemlink Laboratories, Llc | Process for removing water from a functional ingredient composition, and compositions containing the resulting product |
Also Published As
Publication number | Publication date |
---|---|
CA2130002A1 (en) | 1993-08-13 |
US5536430A (en) | 1996-07-16 |
EP0626005A1 (de) | 1994-11-30 |
EP0626005B1 (de) | 1997-12-10 |
DE59307819D1 (de) | 1998-01-22 |
BR9305863A (pt) | 1997-02-18 |
ATE161038T1 (de) | 1997-12-15 |
JPH07503987A (ja) | 1995-04-27 |
AU3496093A (en) | 1993-09-03 |
ES2110596T3 (es) | 1998-02-16 |
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