EP0024711A1 - Produits concentrés de tensides aqueux et procédé pour l'amélioration des propriétés d'écoulement de produits concentrés de tensides aqueux difficilement transportables - Google Patents

Produits concentrés de tensides aqueux et procédé pour l'amélioration des propriétés d'écoulement de produits concentrés de tensides aqueux difficilement transportables Download PDF

Info

Publication number
EP0024711A1
EP0024711A1 EP80105017A EP80105017A EP0024711A1 EP 0024711 A1 EP0024711 A1 EP 0024711A1 EP 80105017 A EP80105017 A EP 80105017A EP 80105017 A EP80105017 A EP 80105017A EP 0024711 A1 EP0024711 A1 EP 0024711A1
Authority
EP
European Patent Office
Prior art keywords
alkyl
viscosity
molecular weight
weight
sulfates
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
EP80105017A
Other languages
German (de)
English (en)
Other versions
EP0024711B2 (fr
EP0024711B1 (fr
Inventor
Uwe Dr. Ploog
Ingo Wegener
Johann Dr. Glasl
Werner Dr. Erwied
Bernhard Bartnick
Rainer Dr. Höfer
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Henkel AG and Co KGaA
Original Assignee
Henkel AG and Co KGaA
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Family has litigation
First worldwide family litigation filed litigation Critical https://patents.darts-ip.com/?family=25780820&utm_source=google_patent&utm_medium=platform_link&utm_campaign=public_patent_search&patent=EP0024711(A1) "Global patent litigation dataset” by Darts-ip is licensed under a Creative Commons Attribution 4.0 International License.
Priority claimed from DE19792935428 external-priority patent/DE2935428A1/de
Priority claimed from DE19803002993 external-priority patent/DE3002993A1/de
Application filed by Henkel AG and Co KGaA filed Critical Henkel AG and Co KGaA
Priority to AT80105017T priority Critical patent/ATE5778T1/de
Publication of EP0024711A1 publication Critical patent/EP0024711A1/fr
Application granted granted Critical
Publication of EP0024711B1 publication Critical patent/EP0024711B1/fr
Publication of EP0024711B2 publication Critical patent/EP0024711B2/fr
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11DDETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
    • C11D3/00Other compounding ingredients of detergent compositions covered in group C11D1/00
    • C11D3/16Organic compounds
    • C11D3/37Polymers
    • C11D3/3703Macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
    • C11D3/3707Polyethers, e.g. polyalkyleneoxides
    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11DDETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
    • C11D1/00Detergent compositions based essentially on surface-active compounds; Use of these compounds as a detergent
    • C11D1/02Anionic compounds
    • C11D1/12Sulfonic acids or sulfuric acid esters; Salts thereof
    • C11D1/123Sulfonic acids or sulfuric acid esters; Salts thereof derived from carboxylic acids, e.g. sulfosuccinates
    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11DDETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
    • C11D1/00Detergent compositions based essentially on surface-active compounds; Use of these compounds as a detergent
    • C11D1/02Anionic compounds
    • C11D1/12Sulfonic acids or sulfuric acid esters; Salts thereof
    • C11D1/14Sulfonic acids or sulfuric acid esters; Salts thereof derived from aliphatic hydrocarbons or mono-alcohols
    • C11D1/146Sulfuric acid esters
    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11DDETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
    • C11D1/00Detergent compositions based essentially on surface-active compounds; Use of these compounds as a detergent
    • C11D1/02Anionic compounds
    • C11D1/12Sulfonic acids or sulfuric acid esters; Salts thereof
    • C11D1/22Sulfonic acids or sulfuric acid esters; Salts thereof derived from aromatic compounds
    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11DDETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
    • C11D1/00Detergent compositions based essentially on surface-active compounds; Use of these compounds as a detergent
    • C11D1/02Anionic compounds
    • C11D1/12Sulfonic acids or sulfuric acid esters; Salts thereof
    • C11D1/29Sulfates of polyoxyalkylene ethers
    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11DDETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
    • C11D17/00Detergent materials or soaps characterised by their shape or physical properties
    • C11D17/0008Detergent materials or soaps characterised by their shape or physical properties aqueous liquid non soap compositions
    • C11D17/003Colloidal solutions, e.g. gels; Thixotropic solutions or pastes
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10STECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S516/00Colloid systems and wetting agents; subcombinations thereof; processes of
    • Y10S516/01Wetting, emulsifying, dispersing, or stabilizing agents
    • Y10S516/03Organic sulfoxy compound containing
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10STECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S516/00Colloid systems and wetting agents; subcombinations thereof; processes of
    • Y10S516/01Wetting, emulsifying, dispersing, or stabilizing agents
    • Y10S516/03Organic sulfoxy compound containing
    • Y10S516/05Organic amine, amide, or n-base containing
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10STECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S526/00Synthetic resins or natural rubbers -- part of the class 520 series
    • Y10S526/911Emulsifying agents

Definitions

  • Alkyl ether sulfates are in particular sulfates of alkoxylated non-aromatic alcohols having 8 to 24 carbon atoms, in particular 8 to 18 carbon atoms.
  • Alcohols of this type can be obtained from raw materials of natural origin, for example coconut or palm kernel oil, or are available as synthetic materials, e.g. in the form of the known Ziegler or oxo alcohols.
  • non-aromatic alcohols with saturated or unsaturated, optionally also branched alkyl radicals of the type mentioned are first alkoxylated to produce detergents with lower alkylene oxides, in particular with ethylene oxide and / or with propylene oxide, then sulfated and then converted into the corresponding water-soluble salts
  • Detergents of this type are used for many purposes, for example in liquid cleaning agents, foam baths and shampoos.
  • Aqueous solutions with a. comparatively low content of alkyl ether sulfate - for example with a content of about 10 wt .-% detergent (WAS) - show the special property of this class of detergents can be thickened by adding neutral salts such as NaCl or Na 2 SO 4 .
  • WAS wt .-% detergent
  • Anionic surfactants also play a dominant role as emulsifiers for the technical production of polymer dispersions.
  • alkyl sulfates, alkyl ether sulfates and alkyl benzene sulfonates, alkylaryl polyglycol ether sulfates and sulfosuccinates of natural and synthetic alcohol polyglycol ethers or alkylphenol ethoxylates are mainly used today.
  • Emulsifiers of the type concerned are usually commercially available in the form of dilute aqueous solutions. Highly concentrated mixtures can only be produced by adding up to 20% lower alcohols such as ethanol or isopropanol.
  • lower alcohols such as ethanol or isopropanol.
  • organic solvents for example the alcohols mentioned, is not always desirable in polymer dispersions for technical reasons, and they are also because of their easy flammability associated with a considerable safety risk both in the manufacture of the emulsifiers and during transport, storage and use. It is also known that even slight shifts in the ratio water / alcohol can result in such concentrates g undesirable Sedimentationserscheinun- s.
  • the object of the invention is to provide aqueous surfactant concentrates of the type described, which can be pumped even in high concentrations and, when diluted with water, show no undesirable increase in the viscosity or thickening of the gel state.
  • the invention aims to provide alcohol-free aqueous surfactant concentrates of alkyl ether sulfates, alkyl aryl ether sulfates, alkyl aryl sulfonates and of sulfosuccinates of alkyl and alkyl aryl polyglycol ether alcohols, as well as fatty alcohols, which can be pumped even in high concentrations, and when diluted with water shows no undesirable increase in the viscosity or thickening of the gel state and without the addition of metal salts, e.g.
  • colloidal gel phases are suitable as detergent surfactants, for shampoo production, for emulsifying natural fats or as polymerization emulsifiers.
  • the formation of colloidal gel phases is to be counteracted in particular. Nevertheless, it should be possible to effectively thicken alkyl ether sulfates in the diluted state at low concentrations of WAS by adding neutral salts such as sodium chloride or sodium sulfate.
  • the technical solution to this problem is based on the finding that water-soluble salts of mono- and / or disulfates of lower polyalkylene ether glycols - in particular of polyethylene glycol and / or of polypropylene glycol (here in particular 1,2-polypropylene glycol) - effective viscosity regulators for aqueous surfactant concentrates here are affected.
  • water-soluble salts of mono- and / or disulfates of lower polyalkylene ether glycols - in particular of polyethylene glycol and / or of polypropylene glycol (here in particular 1,2-polypropylene glycol) - effective viscosity regulators for aqueous surfactant concentrates here are affected.
  • it was found that the effect of these viscosity regulators increases with the increase in the molecular weight of the underlying polyether glycol.
  • the invention relates in a first embodiment to aqueous surfactant concentrates containing at least about 20% by weight of water-soluble salts of one or more of the following surfactants together with small amounts of viscosity regulators: alkyl polyglycol ether sulfates, alkyl aryl polyglycol ether sulfates, alkyl sulfates, alkyl aryl sulfonates, alkyl polyglycol ether sulfosulfinate sulfosate sulfinate sulfosate.
  • surfactant concentrates are characterized in that they contain, as viscosity regulators, water-soluble salts of mono- and / or disulfates of a lower polyalkylene ether glycol with a molecular weight of the polyalkylene ether glycol of at least about 600. If desired, nonionic lower polyalkylene glycols with a molecular weight of at least 1500 can also be used together with the water-soluble salts of the mono- and / or disulfates mentioned for the lower polyalkylene ether glycols.
  • the surfactants are preferably present in amounts of at least about 25% by weight, in particular at least about 30% by weight, e.g. in amounts of 50 to 80% by weight, based on the aqueous surfactant concentrate.
  • Lower polyalkylene ether glycols of the type concerned here are derived from straight-chain or branched glycols having a maximum of up to 5 carbon atoms. Of particular importance have the appropriate polyethylene ether glycols and / or P olypropylenetherglykole - where in the last Fall.der compounds mentioned again, particular from 1,2-propylene glycol derived polyether meaning possess. This information is also valid for the water-soluble salts of the mono- and / or disulfates of the lower polyalkylene ether glycols used as viscosity regulators according to the invention.
  • the invention relates to a process for improving the flow behavior of difficult to move aqueous surfactant concentrates of the type mentioned above in connection with the first embodiment of the invention, this process being characterized in that water-soluble salts of mono- and / or disulfates are used as viscosity regulators uses lower polyalkylene ether glycols with a molecular weight of at least 600, preferably of at least 1000. If desired, the non-sulfated, free, lower polyalkylene ether glycols with a molecular weight of at least 1500 can also be used in the viscosity regulator.
  • the sulfates and here in particular the disulfates of lower polyalkylene ether glycols, in particular of polyethylene oxide and / or of 1,2-polypropylene oxide, have proven to be particularly effective viscosity regulators for highly concentrated aqueous surfactant concentrates of the type concerned by the present invention.
  • the viscosity-reducing effect or the thickening state of the gel of these regulators increases with increasing molecular weight or increasing degree of polycondensation of the alkylene glycol.
  • the molecular weight of the base material for the viscosity regulator is preferably at least about 1000. Molecular weights of up to 6000 or even more can be considered.
  • Disulphates of polyalkylene glycols of the stated type with molecular weights in the range from 1500 to 4000 are particularly preferred.
  • the disulfates used according to the invention as viscosity regulators thus generally originate from polyether glycols which differ from the polyalkylene glycols, as they can be caused by the slight traces of water in the alkoxylation of alcoholic components.
  • the teaching of the invention allows also use the viscosity regulators in a determinable manner according to type and quantity, so that predictable targeted effects with regard to the reduction of the gel state are possible.
  • the viscosity regulators used according to the invention are themselves effective washing-active substances (WAS). An undesirable load with inactive components is avoided.
  • WAS washing-active substances
  • the surfactant mixtures according to the invention can not only be pumped as such in a highly concentrated form, when diluted with water there is no increase in the gel state, but the desired dilution effect.
  • any water-soluble salts of the viscosity regulators used according to the invention can be used.
  • Alkaline salts, soluble alkaline earth metal salts, for example corresponding magnesium salts, the ammonium salts and / or salts with organic amines are particularly suitable for practical use.
  • Suitable amine salts are, for example, alkylolamine salts.
  • the sodium salts are of particular importance.
  • the most important salt for practical use is the sodium salt of the disulfate of polyethylene ether glycols and / or 1,2 polypropylene ether glycols with the minimum molecular weights indicated in each case.
  • the statements made here regarding the salt-forming cations of the viscosity regulators can have corresponding validity for the salt-forming cations present in the surfactants.
  • the viscosity regulators can be present in the aqueous surfactant concentrates in amounts of up to 20% by weight, preferably in amounts of 0.1 to 10% by weight. Amounts of at least 1% by weight, in particular from 2 to 5% by weight, can be particularly preferred. These figures relate to the aqueous surfactant concentrate. In particular, the amount of the viscosity regulator is determined by the desired lowering of the gel point and / or by the thickening effect of the respective surfactant. In terms of the last point of view, the special structure of the surfactant can be significant. If surfactants of the type mentioned are present which contain polyalkoxy radicals, the extent of the polyalkoxylation of the alcohol on which they are based can be significant.
  • low alkoxylated alcohols can usually be effectively influenced even in high concentrations with 2 to 5% by weight of the viscosity regulator, while somewhat larger amounts of the viscosity regulator may be required together with highly polyalkoxylated alcohols (degree of polymerization of the polyalkoxy radical above 10 to 100, for example).
  • free polyethylene glycol and / or free polypropylene glycol can be used together with the sulfates of the polyethylene glycol and / or the polypropylene glycol as a viscosity-regulating component.
  • these non-sulfated polyalkylene ether glycols that effect its appearance more pronounced the higher the molecular weight of the P olyalkylenetherglykols.
  • These free polyalkylene ether glycols which may also be used, should have at least a molecular weight of 1500, preferably their molecular weight is at least 2000 and is, for example, in the range from 2000 to 6000, in particular in the range from 3000 to 5000.
  • the mixing ratio of the sulfates of the lower polyalkylene ether glycols - especially the disulfates - to the free polyalkylene ether glycols is desirably in the range from 1: 0 to 1: 3.
  • the mixing range from 1: 0 to 1: 1 is generally preferred.
  • the viscosity regulator can be added to the aqueous surfactant concentrate as a preformed compound or as a preformed compound mixture.
  • the viscosity regulator is expediently used as a concentrated aqueous solution (content of WAS for example 50 to 90% by weight) and mixed with the aqueous solution of the respective surfactant.
  • the viscosity regulator by sulfating the lower polyalkylene ether glycols in situ in the presence of the surfactant-forming basic components.
  • the sulfation can thus take place, for example, in the presence of an alkyl polyglycol ether alcohol or an alkyl aryl polyglycol ether alcohol.
  • the sulfation of both the alcoholic surfactant-forming component and the preformed lower polyalkylene ether glycols are expediently combined.
  • the desired mixing ratios of the surfactant-forming alcoholic component (s) and the polyalkylene ether glycols forming the viscosity regulator are simply set here and then this mixture of substances is subjected to the sulfation known per se. Finally, the sulfates formed are converted into the desired water-soluble salt. The same cation is set in the surfactant and in the viscosity regulator.
  • alkyl ether sulfates are sulfates of alkoxylated C 8 -C 24 alcohols, preferably such derivatives with a carbon chain of 8 to 18 carbon atoms.
  • Non-aromatic alcohols with carbon chains of 10 to 16 links can be particularly preferred.
  • the carbon chain can be straight-chain and / or branched and saturated and / or unsaturated.
  • alcohols of the type mentioned are accessible both from natural products and by synthesis.
  • the alcohols are alkoxylated with lower alkylene oxides.
  • the low alkoxylated derivatives up to 10 or 12, preferably 1 to 4, in particular 2 to 3, alkoxy groups are added to the alcohol radical.
  • the highly alkoxylated derivatives polyalkoxy radicals with a number of members over 10 or 12, for example up to 100, in particular 20 to 80, are provided.
  • the most important alkoxylating agents are ethylene oxide and / or 1,2-propylene oxide.
  • Suitable as a group of suitable water-soluble salts of the sulfated polyalkoxylated compounds is the one mentioned above in connection with the viscosity regulator Group of cations.
  • Suitable salts are therefore in particular the alkali metal salts, soluble alkaline earth metal salts, ammonium salts and salts with organic amines.
  • the most important salt in practice is the sodium salt of alkyl ether sulfate.
  • the preferred surfactants of this class can be represented by the general formula
  • R alkyl radical which can be straight-chain or branched and can be saturated or unsaturated. Alkyl radicals having 4 to 16 carbon atoms, in particular having 6 to 14 carbon atoms, are preferred here. Alkyl radicals with 8 to 12 carbon atoms can be of particular importance.
  • n 1 or 2, 1 being preferred as a rule.
  • A lower alkylene radical, which can be straight-chain and / or branched.
  • the preferred lower alkylene radicals are ethylene and / or propylene (1,2).
  • n 1 to 100.
  • low alkoxylated derivatives up to 12 ins special 2 to 10 alkoxy groups added to the alcohol residue.
  • polyalkoxy radicals with a number of members greater than 12, for example up to 100, in particular 20 to 50, are provided.
  • M cation of a soluble salt, in particular alkali, water-soluble alkaline earth, ammonium or organic amines. The most preferred cation is sodium.
  • the compounds preferably correspond to the general formula
  • R-O- residue of a non-aromatic alcohol which can be straight-chain or branched and can be saturated or unsaturated and generally has 8 to 24 carbon atoms, preferably 10 to 18 carbon atoms.
  • Ar phenylene or naphthylene, the phenylene radical is preferred
  • the S0 3M group can also be interchanged within the succinic acid residue.
  • this alkyl radical preferably contains at least 8 carbon atoms, radicals with 10 to 18 carbon atoms can be particularly preferred.
  • A lower alkylene radical, which can be straight-chain and / or branched.
  • the Favor q th Alkvlenreste are
  • n is preferably 1 to 12, in particular 2 to 10.
  • n has a value> 12 to in particular 100, preferably 20 to 50.
  • the sulfonic acid residue in succinic acid may also be interchanged in surfactants of this type.
  • the diester of sulfosuccinic acid is again present.
  • Z -OM or -OR (diester of sulfosuccinic acid)
  • aqueous surfactant concentrates according to the invention can also contain other surface-active agents.
  • nonionic WAS for example alkylphenol polyglycol ethers, are suitable.
  • inorganic salts such as sodium chloride and / or sodium sulfate are usually present in the aqueous concentrates of the invention from the preparation of the alkyl and alkylaryl ether sulfates and the sulfosuccinates described and / or the viscosity regulators used according to the invention, see also the statements relating to the prior art.
  • Na-C12 / 14-fatty alcohol-2-EO sulfate is used as the surfactant in the starting solution.
  • Surfactant used Na-C12 / 14-fatty alcohol-2-EO-sulfate
  • Na-C12 / 14-2 sulfate is liquefied with 3% by weight or 6% by weight of the viscosity regulator and after dilution with water to a content of 10% by weight WAS is examined for its thickenability with sodium chloride.
  • WAS a content of 10% by weight
  • Tables a) and b) show that even small amounts of the viscosity regulators according to the invention have a liquefying effect on highly concentrated fatty alcohol ether sulfates. At the transition to lower concentrations i.e. when diluted, the viscosity is not increased abruptly, but a decrease occurs.
  • An adduct of 50 moles of ethylene oxide with one mole of C12 / 14 fatty alcohol is sulfated with chlorosulfonic acid alone and in the blends with polyethylene glycol given in Table 6 under customary conditions. 1.05 moles of chlorosulfonic acid are used per mole of hydroxyl groups (calculated according to the OH number). After neutralizing with sodium hydroxide solution and setting an active substance concentration of 25% by weight, the gel points listed in Table 6 are found.
  • This example explains the use of polyglycols or polyglycol disulfates to lower the gel point of a highly ethoxylated alkylphenol ether sulfate.
  • the aqueous solution of a dodecylphenol + 40 EO sulfate, Na salt, with an active substance content of 30% by weight has a gel point of +12.5 o C. To lower the gel point, are used.
  • the Höppler viscosity at 25 ° C of a 30% C 12 / C 15 oxo alcohol sulfate Na salt (abbreviated here with OAS) is approx. 8500 mPa ⁇ s.
  • OAS oxo alcohol sulfate Na salt
  • the viscosity-breaking influence of PEG disulfates on such aqueous alkyl sulfate concentrates is determined.
  • the following blends are made by OAS and the Höppler viscosity is measured.
  • ABS 50% n-dodecylbenzenesulfonate
  • Viscosity-breaking influence of polyethylene glycols and PEG disulfates on such aqueous ABS concentrates determined.
  • the following mixes of ABS are produced and the Höppler viscosity is measured.
  • the di-Na-sulfosuccinic acid half-ester of octylphenol + 11 EO forms a non-pourable, immobile gel at 30% AS in aqueous solution, which only becomes fluid at 33 ° C (gel point).
  • the Höppler viscosity of the gel at 25 ° C is naturally not measurably high.
  • the gel point can be reduced to -2 ° C, the Höppler viscosity at 25 ° C is measurable and is only 80 - 100 mPa s.
  • 10% PEG 4000 disulphate, Na salt, as a 33% aqueous solution the gel point can be reduced even further and is then ⁇ -10 ° C.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Wood Science & Technology (AREA)
  • Organic Chemistry (AREA)
  • Dispersion Chemistry (AREA)
  • Detergent Compositions (AREA)
EP80105017A 1979-09-01 1980-08-23 Produits concentrés de tensides aqueux et procédé pour l'amélioration des propriétés d'écoulement de produits concentrés de tensides aqueux difficilement transportables Expired EP0024711B2 (fr)

Priority Applications (1)

Application Number Priority Date Filing Date Title
AT80105017T ATE5778T1 (de) 1979-09-01 1980-08-23 Waessrige tensidkonzentrate und verfahren zur verbesserung des fliessverhaltens schwer beweglicher waessriger tensidkonzentrate.

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
DE19792935428 DE2935428A1 (de) 1979-09-01 1979-09-01 Waessrige tensidkonzentrate und verfahren zur verbesserung des fliessverhaltens schwer beweglicher waessriger tensidkonzentrate
DE2935428 1979-09-01
DE3002993 1980-01-29
DE19803002993 DE3002993A1 (de) 1980-01-29 1980-01-29 Waessrige tensidkonzentrate und verfahren zur verbesserung des fliessverhaltens schwerbeweglicher waessriger tensidkonzentrate

Publications (3)

Publication Number Publication Date
EP0024711A1 true EP0024711A1 (fr) 1981-03-11
EP0024711B1 EP0024711B1 (fr) 1984-01-04
EP0024711B2 EP0024711B2 (fr) 1989-02-08

Family

ID=25780820

Family Applications (1)

Application Number Title Priority Date Filing Date
EP80105017A Expired EP0024711B2 (fr) 1979-09-01 1980-08-23 Produits concentrés de tensides aqueux et procédé pour l'amélioration des propriétés d'écoulement de produits concentrés de tensides aqueux difficilement transportables

Country Status (4)

Country Link
US (2) US4384978A (fr)
EP (1) EP0024711B2 (fr)
CA (1) CA1152850A (fr)
DE (1) DE3066054D1 (fr)

Cited By (19)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0084154A1 (fr) * 1981-12-28 1983-07-27 Henkel Kommanditgesellschaft auf Aktien Utilisation de régulateurs de viscosité pour concentrats tensio-actifs
US4495092A (en) * 1983-02-17 1985-01-22 Henkel Kommanditgesellschaft Auf Aktien Viscosity regulators for high-viscosity surfactant concentrates
US4532076A (en) * 1982-02-11 1985-07-30 Henkel Kommanditgesellschaft Auf Aktien Aqueous anionic surfactant concentrates containing viscosity reducing agents
EP0059043B1 (fr) * 1981-02-19 1985-08-21 Imperial Chemical Industries Plc Compositions tensio-actives
EP0222557A2 (fr) 1985-10-31 1987-05-20 The Procter & Gamble Company Composition détergente liquide
US4904359A (en) * 1985-10-31 1990-02-27 The Procter & Gamble Company Liquid detergent composition containing polymeric surfactant
EP0359308A2 (fr) * 1988-09-16 1990-03-21 Unilever N.V. Compositions détergentes liquides
EP0401642A1 (fr) * 1989-06-05 1990-12-12 Henkel Kommanditgesellschaft auf Aktien Sulfates d'alkyle gras et sulfates d'éthers alkyliques gras du polyalkylène glycol, procédé pour leur préparation et leur utilisation
WO1991006623A1 (fr) * 1989-10-31 1991-05-16 Unilever N.V. Compositions detergentes
EP0431653A2 (fr) * 1989-08-31 1991-06-12 Shell Internationale Researchmaatschappij B.V. Composition liquide tensio-active
WO1991019775A1 (fr) * 1990-06-15 1991-12-26 Henkel Kommanditgesellschaft Auf Aktien Utilisation de sels des produits de sulfonation d'acides gras insatures comme reducteurs de viscosite
WO1992006952A1 (fr) * 1990-10-17 1992-04-30 Henkel Kommanditgesellschaft Auf Aktien Procede de production de pates de sulfate d'alkyle a fluidite amelioree
WO1992007054A1 (fr) * 1990-10-17 1992-04-30 Henkel Kommanditgesellschaft Auf Aktien Procede de production de pates en sulfate d'alkyle a fluidite amelioree
EP0618000A1 (fr) * 1992-08-06 1994-10-05 Air Products And Chemicals, Inc. Compositions tensioactives hydrosolubles
WO1995004035A1 (fr) * 1993-08-02 1995-02-09 Henkel Kommanditgesellschaft Auf Aktien Formulations liquides renfermant un diester de l'acide sulfosuccinique
US5446188A (en) * 1991-03-21 1995-08-29 Henkel Kommanditgesellschaft Auf Aktien Process for the production of highly concentrated fatty alcohol sulfate pastes
US5538672A (en) * 1991-08-03 1996-07-23 Henkel Kommanditgesellschaft Auf Aktien Free-flowing water-containing alkyl sulfate pastes
DE102011015046A1 (de) * 2011-03-24 2012-09-27 Sasol Germany Gmbh Hochkonzentrierte fließfähige Salze von Alkylpolyalkoxysulfaten
WO2014072840A1 (fr) 2012-11-12 2014-05-15 Galaxy Surfactants Ltd. Sulfates d'alkyle gras aqueux hautement actifs fluides

Families Citing this family (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0024711B2 (fr) * 1979-09-01 1989-02-08 Henkel Kommanditgesellschaft auf Aktien Produits concentrés de tensides aqueux et procédé pour l'amélioration des propriétés d'écoulement de produits concentrés de tensides aqueux difficilement transportables
GB8404120D0 (en) * 1984-02-16 1984-03-21 Unilever Plc Liquid detergent compositions
DE3447859A1 (de) * 1984-12-31 1986-07-10 Henkel KGaA, 4000 Düsseldorf Verwendung von alkansulfonaten als viskositaetsregler fuer hochviskose aniontensid-konzentrate
US4765926A (en) * 1986-03-18 1988-08-23 Vista Chemical Company Surfactant compositions and method therefor
DE3622438A1 (de) * 1986-07-04 1988-01-07 Henkel Kgaa Kosmetischer waschrohstoff
DE3630533A1 (de) * 1986-09-08 1988-03-10 Henkel Kgaa Neue tensidgemische und ihre verwendung
US4758374A (en) * 1987-03-17 1988-07-19 Conoco Inc. Soluble oil concentrate and emulsifier system used therein
GB8718217D0 (en) * 1987-07-31 1987-09-09 Unilever Plc Liquid detergent compositions
GB2223611A (en) * 1988-10-07 1990-04-11 Nigel Anthony Collier Electronic bark suppressor
DE4024657A1 (de) * 1990-08-03 1992-02-06 Henkel Kgaa Verfahren zur trocknung und granulierung waessriger pasten waschaktiver wirkstoffgemische
US5529722A (en) * 1992-03-10 1996-06-25 The Procter & Gamble Company High active detergent pastes
ES2131524T3 (es) * 1992-03-10 1999-08-01 Procter & Gamble Pastas detergentes muy activas.
WO1996025482A1 (fr) * 1995-02-13 1996-08-22 The Procter & Gamble Company Procede pour produire des agglomerats detergents a classe granulometrique controlee
US5574005A (en) * 1995-03-07 1996-11-12 The Procter & Gamble Company Process for producing detergent agglomerates from high active surfactant pastes having non-linear viscoelastic properties
ES2328632T3 (es) * 2005-11-15 2009-11-16 The Procter And Gamble Company Composicon detergente liquida con tensioactivo alquil o hidroxialquil sulfato o sulfonato de origen natural y tensoactivos oxido de amina ramificados en mitad de la cadena.
CN113717008B (zh) * 2021-08-13 2022-10-14 四川鸿康科技股份有限公司 一种磷酸一铵防结块剂及其应用

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2305554A1 (de) * 1972-02-07 1973-08-23 Albright & Wilson Komponenten fuer waessrige detergentkonzentrate
FR2268069A1 (fr) * 1974-04-19 1975-11-14 Procter & Gamble Europ
DE2550341A1 (de) * 1974-11-13 1976-05-20 Procter & Gamble Niederviskoses waschaktives saeuregemisch
DE2501982A1 (de) * 1975-01-18 1976-07-22 Bayer Ag Konzentrierte fluessige einstellungen von alkylsulfonaten und ihre mischungen mit polyglykolaethern
DE2703998A1 (de) * 1977-02-01 1978-08-03 Henkel Kgaa Fluessiges waschmittelkonzentrat mit geringem schaumvermoegen

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1970578A (en) * 1930-11-29 1934-08-21 Ig Farbenindustrie Ag Assistants for the textile and related industries
US2758977A (en) * 1951-05-25 1956-08-14 Gen Aniline & Film Corp Detergent composition and method of producing same
US2940936A (en) * 1953-04-07 1960-06-14 Monsanto Chemicals Preparing sulfonated products from sulfur trioxide
BE790362A (fr) * 1971-10-20 1973-02-15 Albright & Wilson Composants de detergents
GB1437089A (en) 1972-05-26 1976-05-26 Albright & Wilson Detergent concentrates
EP0024711B2 (fr) * 1979-09-01 1989-02-08 Henkel Kommanditgesellschaft auf Aktien Produits concentrés de tensides aqueux et procédé pour l'amélioration des propriétés d'écoulement de produits concentrés de tensides aqueux difficilement transportables

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2305554A1 (de) * 1972-02-07 1973-08-23 Albright & Wilson Komponenten fuer waessrige detergentkonzentrate
FR2268069A1 (fr) * 1974-04-19 1975-11-14 Procter & Gamble Europ
DE2550341A1 (de) * 1974-11-13 1976-05-20 Procter & Gamble Niederviskoses waschaktives saeuregemisch
DE2501982A1 (de) * 1975-01-18 1976-07-22 Bayer Ag Konzentrierte fluessige einstellungen von alkylsulfonaten und ihre mischungen mit polyglykolaethern
DE2703998A1 (de) * 1977-02-01 1978-08-03 Henkel Kgaa Fluessiges waschmittelkonzentrat mit geringem schaumvermoegen

Cited By (27)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0059043B1 (fr) * 1981-02-19 1985-08-21 Imperial Chemical Industries Plc Compositions tensio-actives
EP0084154A1 (fr) * 1981-12-28 1983-07-27 Henkel Kommanditgesellschaft auf Aktien Utilisation de régulateurs de viscosité pour concentrats tensio-actifs
US4532076A (en) * 1982-02-11 1985-07-30 Henkel Kommanditgesellschaft Auf Aktien Aqueous anionic surfactant concentrates containing viscosity reducing agents
US4495092A (en) * 1983-02-17 1985-01-22 Henkel Kommanditgesellschaft Auf Aktien Viscosity regulators for high-viscosity surfactant concentrates
EP0222557A2 (fr) 1985-10-31 1987-05-20 The Procter & Gamble Company Composition détergente liquide
EP0222557A3 (en) * 1985-10-31 1988-09-28 The Procter & Gamble Company Liquid detergent composition
US4904359A (en) * 1985-10-31 1990-02-27 The Procter & Gamble Company Liquid detergent composition containing polymeric surfactant
EP0359308A2 (fr) * 1988-09-16 1990-03-21 Unilever N.V. Compositions détergentes liquides
EP0359308A3 (fr) * 1988-09-16 1991-01-16 Unilever N.V. Compositions détergentes liquides
EP0401642A1 (fr) * 1989-06-05 1990-12-12 Henkel Kommanditgesellschaft auf Aktien Sulfates d'alkyle gras et sulfates d'éthers alkyliques gras du polyalkylène glycol, procédé pour leur préparation et leur utilisation
WO1990015049A1 (fr) * 1989-06-05 1990-12-13 Henkel Kommanditgesellschaft Auf Aktien Alkylsulfates gras et alkylpolyalkylene-glycolethersulfates gras; leur procede de production et leur utilisation
EP0431653A2 (fr) * 1989-08-31 1991-06-12 Shell Internationale Researchmaatschappij B.V. Composition liquide tensio-active
EP0431653A3 (en) * 1989-08-31 1993-03-10 Shell Internationale Research Maatschappij B.V. Liquid surface active compositions
WO1991006623A1 (fr) * 1989-10-31 1991-05-16 Unilever N.V. Compositions detergentes
WO1991019775A1 (fr) * 1990-06-15 1991-12-26 Henkel Kommanditgesellschaft Auf Aktien Utilisation de sels des produits de sulfonation d'acides gras insatures comme reducteurs de viscosite
WO1992006952A1 (fr) * 1990-10-17 1992-04-30 Henkel Kommanditgesellschaft Auf Aktien Procede de production de pates de sulfate d'alkyle a fluidite amelioree
WO1992007054A1 (fr) * 1990-10-17 1992-04-30 Henkel Kommanditgesellschaft Auf Aktien Procede de production de pates en sulfate d'alkyle a fluidite amelioree
US5304669A (en) * 1990-10-17 1994-04-19 Henkel Kommanditgesellschaft Auf Aktien Process for the production of alkyl sulfate pastes having improved flow properties
US5446188A (en) * 1991-03-21 1995-08-29 Henkel Kommanditgesellschaft Auf Aktien Process for the production of highly concentrated fatty alcohol sulfate pastes
US5538672A (en) * 1991-08-03 1996-07-23 Henkel Kommanditgesellschaft Auf Aktien Free-flowing water-containing alkyl sulfate pastes
EP0618000A1 (fr) * 1992-08-06 1994-10-05 Air Products And Chemicals, Inc. Compositions tensioactives hydrosolubles
WO1995004035A1 (fr) * 1993-08-02 1995-02-09 Henkel Kommanditgesellschaft Auf Aktien Formulations liquides renfermant un diester de l'acide sulfosuccinique
US5908582A (en) * 1993-08-02 1999-06-01 Henkel Kommanditgesellschaft Auf Aktien Liquid formulations containing sulfosuccinic acid diester
DE102011015046A1 (de) * 2011-03-24 2012-09-27 Sasol Germany Gmbh Hochkonzentrierte fließfähige Salze von Alkylpolyalkoxysulfaten
EP2688977B1 (fr) 2011-03-24 2017-11-01 SASOL Germany GmbH Sels de sulfates d'alkylpolyalcoxy très concentrés doués d'écoulement
EP2688977B2 (fr) 2011-03-24 2020-06-03 SASOL Germany GmbH Sels de sulfates d'alkylpolyalcoxy très concentrés doués d'écoulement
WO2014072840A1 (fr) 2012-11-12 2014-05-15 Galaxy Surfactants Ltd. Sulfates d'alkyle gras aqueux hautement actifs fluides

Also Published As

Publication number Publication date
CA1152850A (fr) 1983-08-30
EP0024711B2 (fr) 1989-02-08
DE3066054D1 (en) 1984-02-09
US4476037A (en) 1984-10-09
US4384978A (en) 1983-05-24
EP0024711B1 (fr) 1984-01-04

Similar Documents

Publication Publication Date Title
EP0024711B1 (fr) Produits concentrés de tensides aqueux et procédé pour l'amélioration des propriétés d'écoulement de produits concentrés de tensides aqueux difficilement transportables
EP0116905B1 (fr) Utilisation de dérivés d'alcools comme régleurs de la viscosité pour des concentrés de tensio-actifs techniques hautement visqueux
EP0084154B1 (fr) Utilisation de régulateurs de viscosité pour concentrats tensio-actifs
DE3638314A1 (de) Klare, waessrige waschmittelzusammensetzungen
DE2110030A1 (de) Flüssigwaschmittel
WO1995021905A1 (fr) Produit de nettoyage de surfaces dures
EP0608285B2 (fr) Preparations tensioactives visqueuses aqueuses
DE2632953A1 (de) Reinigungsmittelgemisch, enthaltend ein alkylaethersulfat-detergens
EP0574448A1 (fr) Detergents liquides a teneur en disels d'acide sulfo-oleique
DE3724500A1 (de) Alkylsulfat-ethersulfat-gemische und deren verwendung
WO2000071665A1 (fr) Nettoyant aqueux acide a plusieurs phases
DE2935428A1 (de) Waessrige tensidkonzentrate und verfahren zur verbesserung des fliessverhaltens schwer beweglicher waessriger tensidkonzentrate
WO1992014809A1 (fr) Procede de production de pates de sulfate d'alkyle et/ou d'alcenyle a fluidite amelioree
EP0103696B1 (fr) Concentrés aqueux de tenside et procédé pour l'écoulement de concentrés aqueux de tenside de faible fluidité
DE2819455A1 (de) Fluessiges waschmittel und verfahren zu seiner herstellung
DE60101225T2 (de) Hoch schäumende reinigungsmittel für harte oberflächen
DE3002993A1 (de) Waessrige tensidkonzentrate und verfahren zur verbesserung des fliessverhaltens schwerbeweglicher waessriger tensidkonzentrate
EP0670877B1 (fr) Preparations tensioactives visqueuses aqueuses
DE2817626C2 (fr)
EP0975719B1 (fr) Procede de preparation des pates aqueuses d'alkyl(ether)sulfate a basse viscosite et a haute concentration
DE2438136A1 (de) Reinigungsmittelmischung
DE3916628A1 (de) Verdickungsmittel fuer waessrige tensidloesungen
WO1996037590A1 (fr) Composition detergente aqueuse
CH458385A (de) Verfahren zur Herstellung von neuen Additionsverbindungen aus kapillaraktiven Schwefelsäurehalbestern bzw. deren Salzen und Sulfobetainen
DE1257339B (de) Waessrige Fluessigwaschmittel mit einem Gehalt an celluloseaethercarbonsauren Salzen

Legal Events

Date Code Title Description
PUAI Public reference made under article 153(3) epc to a published international application that has entered the european phase

Free format text: ORIGINAL CODE: 0009012

AK Designated contracting states

Designated state(s): AT BE CH DE FR GB IT NL SE

17P Request for examination filed

Effective date: 19810727

ITF It: translation for a ep patent filed

Owner name: STUDIO JAUMANN

GRAA (expected) grant

Free format text: ORIGINAL CODE: 0009210

AK Designated contracting states

Designated state(s): AT BE CH DE FR GB IT LI NL SE

REF Corresponds to:

Ref document number: 5778

Country of ref document: AT

Date of ref document: 19840115

Kind code of ref document: T

REF Corresponds to:

Ref document number: 3066054

Country of ref document: DE

Date of ref document: 19840209

ET Fr: translation filed
PLBI Opposition filed

Free format text: ORIGINAL CODE: 0009260

PLBI Opposition filed

Free format text: ORIGINAL CODE: 0009260

26 Opposition filed

Opponent name: CHEMISCHE WERKE HUELS AG

Effective date: 19840918

26 Opposition filed

Opponent name: HOECHST AKTIENGESELLSCHAFT, FRANKFURT

Effective date: 19841003

PLAB Opposition data, opponent's data or that of the opponent's representative modified

Free format text: ORIGINAL CODE: 0009299OPPO

PLAB Opposition data, opponent's data or that of the opponent's representative modified

Free format text: ORIGINAL CODE: 0009299OPPO

R26 Opposition filed (corrected)

Opponent name: HUELS AKTIENGESELLSCHAFT * 841003 HOECHST AKTIENGE

Effective date: 19840918

R26 Opposition filed (corrected)

Opponent name: HUELS AKTIENGESELLSCHAFT * 841003 HOECHST AKTIENGE

Effective date: 19840918

NLXE Nl: other communications concerning ep-patents (part 3 heading xe)

Free format text: SHOULD BE MODIFIED INTO:HUELS AKTIENGESELLSCHAFT

PUAH Patent maintained in amended form

Free format text: ORIGINAL CODE: 0009272

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: PATENT MAINTAINED AS AMENDED

27A Patent maintained in amended form

Effective date: 19890208

AK Designated contracting states

Kind code of ref document: B2

Designated state(s): AT BE CH DE FR GB IT NL SE

ET3 Fr: translation filed ** decision concerning opposition
NLR2 Nl: decision of opposition
ITF It: translation for a ep patent filed

Owner name: STUDIO JAUMANN

NLR3 Nl: receipt of modified translations in the netherlands language after an opposition procedure
ITTA It: last paid annual fee
PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: CH

Payment date: 19940718

Year of fee payment: 15

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: AT

Payment date: 19940727

Year of fee payment: 15

EAL Se: european patent in force in sweden

Ref document number: 80105017.0

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: SE

Payment date: 19950816

Year of fee payment: 16

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: AT

Effective date: 19950823

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: LI

Effective date: 19950831

Ref country code: CH

Effective date: 19950831

REG Reference to a national code

Ref country code: CH

Ref legal event code: PL

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: SE

Effective date: 19960824

EUG Se: european patent has lapsed

Ref document number: 80105017.0

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: FR

Payment date: 19970811

Year of fee payment: 18

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: FR

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 19990430

REG Reference to a national code

Ref country code: FR

Ref legal event code: ST

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: GB

Payment date: 19990818

Year of fee payment: 20

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: DE

Payment date: 19990823

Year of fee payment: 20

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: NL

Payment date: 19990830

Year of fee payment: 20

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: BE

Payment date: 19991013

Year of fee payment: 20

BE20 Be: patent expired

Free format text: 20000823 *HENKEL K.G.A.A.

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: GB

Free format text: LAPSE BECAUSE OF EXPIRATION OF PROTECTION

Effective date: 20000822

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: NL

Free format text: LAPSE BECAUSE OF EXPIRATION OF PROTECTION

Effective date: 20000823

REG Reference to a national code

Ref country code: GB

Ref legal event code: PE20

Effective date: 20000822

NLV7 Nl: ceased due to reaching the maximum lifetime of a patent

Effective date: 20000823