DK156274B - DIFFICULT TENSID CONCENTRATES - Google Patents

DIFFICULT TENSID CONCENTRATES Download PDF

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DK156274B
DK156274B DK335180AA DK335180A DK156274B DK 156274 B DK156274 B DK 156274B DK 335180A A DK335180A A DK 335180AA DK 335180 A DK335180 A DK 335180A DK 156274 B DK156274 B DK 156274B
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weight
viscosity
salts
molecular weight
water
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DK335180AA
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DK335180A (en
DK156274C (en
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Uwe Ploog
Ingo Wegener
Johann Glasl
Werner Erwied
Bernhard Bartnick
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Henkel Kgaa
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    • 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
    • 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

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  • 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)
  • Detergent Compositions (AREA)
  • Emulsifying, Dispersing, Foam-Producing Or Wetting Agents (AREA)
  • Manufacture And Refinement Of Metals (AREA)

Description

DK 156274 BDK 156274 B

Fremstillingen af pumpbare h0jkoncentrerede alkylethersulfater frembyder som tidligere kendt et problem, der er vanske-ligt at l0se. Alkylethersulfater er i denne forbindelse især sulfater af alkoxylerede ikke-aromatiske âlkoholer xned 8 til 24 5 carbonatomer, især 8 til 18 carbonatomer. Âlkoholer af denne art kan udvindes af udgangsmaterialer af naturlig oprindelse, eksempelvis kokosn0d- eller palmekerneolie, eller star til râdighed som syntetisk materiale, f.eks. i form af de kendte Ziegler- eller oxo-âlkoholer. De ikke-aromatiske âlkoholer 10 med mættede eller umættede, eventuelt ogsâ forgrenede alkyl= grupper af den nævnte art bliver med henblik pâ fremstilling af detergenter til at begynde med alkoxyleret med lavere al= kylenoxider, især med ethylenoxid og/eller med propylenoxid, og derpâ sulfateret samt derpâ omdannet til de tilsvarende 15 vandopl0selige salte.The preparation of pumpable high-concentrated alkyl ether sulfates presents, as previously known, a problem which is difficult to solve. Alkyl ether sulphates are in this connection especially sulphates of alkoxylated non-aromatic alcohols containing from 8 to 24 carbon atoms, especially from 8 to 18 carbon atoms. Alcohols of this kind can be extracted from starting materials of natural origin, for example coconut or palm kernel oil, or available as synthetic material, e.g. in the form of the known Ziegler or oxo alcohols. The non-aromatic alcohols 10 with saturated or unsaturated, optionally also branched alkyl = groups of the aforementioned kind are made for the purpose of producing detergents to begin with alkoxylated with lower alkylene oxides, especially with ethylene oxide and / or with propylene oxide, and thereafter sulfated and then converted to the corresponding 15 water-soluble salts.

Detergenter af denne art finder mangeartet anvendelse, eksempelvis i flydende rensemidler, skumbade og hârvaskemidler.Detergents of this kind find many uses, for example in liquid cleaners, foam baths and hair washing agents.

Vandige opl0sninger med et forholdsvis ringe indhold af al= kylethersulfat - eksempelvis med et indhold pâ ca. 10 vægt% 20 vaskeaktivt materiale (WAS) - udviser denne detergent-stof-klasses særlige egenskab atter at kunne fortykkes ved til-sætning af neutrale salte, sâsom NaCl eller Na2S0^. I praksis g0res der hyppigt brug af denne egenskab ved den her omhand-lede klasse detergenter.Aqueous solutions having a relatively low content of alkyl ether sulphate - for example having a content of approx. 10 wt% 20 detergent (WAS) - exhibits the particular property of this detergent class again to be thickened by the addition of neutral salts, such as NaCl or Na 2 SO 4. In practice, this property is frequently used in the class of detergents in question.

25 En yderligere særegenhed i de rheologiske forhold hos tilsvarende tensidkoncentrater medf0rer imidlertid tungtvejende vanskeligheder for den praktiske anvendelighed. H0jkoncen-trerede vandige tensidkoncentrater med et WAS-indhold pâ eksempelvis 50 vægt% eller mere har konsistens som en tyk 30 gel eller en tilsvarende pasta og er ikke pumpbar. Fors0ger man at fortynde denne gel med vand, synker fortykkelsestil-standen ikke i noget forventet omfang, men stiger tværtimod til at begynde med. Forstâeligt nok opstâr der herved betyde-lige problemer for den, der skal viderebehandle materialet.25 A further peculiarity in the rheological conditions of corresponding surfactant concentrates, however, entails considerable difficulties in practical application. Highly concentrated aqueous surfactant concentrates having a WAS content of, for example, 50% by weight or more have consistency as a thick 30 gel or similar paste and are not pumpable. If one tries to dilute this gel with water, the thickening state does not decrease to any expected extent, but on the contrary increases initially. Understandably, this creates significant problems for the person who needs to process the material.

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Der foreligger de inest forskellige forslag til overvindelse af denne vanskelighed. Tilsætning af begrænsede mængder af de forskellige komponenter som viskositetsregula- torer til det vandige tensidkoncentrat kendes. Der henvises 5 her til tysk offentligg0relsesskrift nr. 2.251.405 (bestemte carboxylsyresalte, især salte af hydroxycarboxylsyrer), tysk offentligg0relsesskrift nr. 2,305.554 (tilsætning af aroma-tiske sulfonsyrer eller de vandop10selige salte deraf) samt tysk offentligg0relsesskrift nr. 2.326.006 (sulfonsyrer eller 10 sulfater eller de tilsvarende vandopl0selige salte af jmættede eller umættede alifatiske hydrocarbongrupper eller hydrocar= bonoxy-hydroc arbongrupper med 1 til 6 c arb on a t orner, der ogsâ kan være substitueret pâ bestemt mâde). If01ge angivelserne i disse trykskrifter er tilsætningen af lavere alkoholer, sâ-15 som isopropanol eller éthanol, kendt i praksis til l0sning af det ovenfor omtalte problem. De lavere alkoholer medf0rer imidlertid tungtvejende ulemper som f01ge af de h0je damptryk og deres antændelighed.There are the innumerable suggestions for overcoming this difficulty. Addition of limited amounts of the various components as viscosity regulators to the aqueous surfactant concentrate is known. Reference is made here to German Publication No. 2,251,405 (certain carboxylic acid salts, in particular salts of hydroxycarboxylic acids), German Publication No. 2,305,554 (addition of aromatic sulfonic acids or the water-soluble salts thereof), and German publication No. 32 32 or 10 sulphates or the corresponding water-soluble salts of unsaturated or unsaturated aliphatic hydrocarbon groups or hydrocarbon bonoxy-hydrocarbon groups having 1 to 6 c of carbon, which may also be substituted in a specific way). According to the disclosures in these printing presses, the addition of lower alcohols, such as isopropanol or ethanol, is known in practice to solve the above-mentioned problem. However, the lower alcohols cause significant disadvantages as a result of the high vapor pressure and their flammability.

Den foreliggende opfindelse tager sigte pâ at tilveje- 2.0 bringe vandige tensidkoncentrater af de nævnte alkyl= ethersulfater, som ogsâ er pumpbare i h0je koncentrationer, og som ved fortynding med vand ikke udviser nogen u0nsket stigning i viskositeten eller fortykkelse af geltilstanden og alligevel i fortyndet tilstand i tilfælde af lave WAS-25 koncentrationer kan fortykkes virkningsfuldt ved tilsætning af neutrale salte, sâsom natriumchlorid eller natriumsulfat.The present invention is intended to provide 2.0 aqueous surfactant concentrates of said alkyl ether sulfates which are also pumpable at high concentrations and which, upon dilution with water, show no undesirable increase in viscosity or thickening of the gel state and yet in diluted state. in the case of low WAS-25 concentrations, it can be effectively thickened by the addition of neutral salts, such as sodium chloride or sodium sulfate.

Den tekniske 10sning af denne opgave gâr ud fra den konsta-tering, at vandop10selige salte af mono- og/eller disulfater af lavere polyalkylenglycoler - især af polyethylenglycol· 30 og/eller polypropylenglycol. - er virkningsfulde viskositets-regulatorer for vandige tensidkoncentrater af den her omhand-lede art. Der blev herved gjort brug af den konstatering, at virkningen af disse viskositetsregulatorer tiltager med stig-ningen i molekylvægten af den grundlæggende polyetherglycol.The technical solution of this task is based on the finding that water-soluble salts of mono- and / or disulfates of lower polyalkylene glycols - especially of polyethylene glycol · 30 and / or polypropylene glycol. - are effective viscosity controllers for aqueous surfactant concentrates of the kind in question. It was thereby used to find that the effect of these viscosity regulators increases with the increase in the molecular weight of the basic polyether glycol.

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Den foreliggende opfindelse angâr felgelig vandige tensidkon-centrater indeholdende 25-80 vægt% vandoplosel ige salte af alifatiske alkoxylerede og derefter sulfaterede alkoholer (ethersulfatsalte) sammen med ringe mængder viskositetsregu-5 latorer. Disse tensidkoncentrater er ejendommelige ved, at de soin viskositetsregulatorer indeholder 1-10 vægt% vandoplose-lige alkalimetal-, ammonium- og/eller aminsalte af disulfater af polyethylenglycol og/eller af polypropylenglycol med en molekylvægt af polyalkylenetherglycolen pâ 600-6000, om onsket 10 sammen med lavere polyalkylenetherglycoler med en molekylvægt pâ 1500-6000 i mængdeforhold 1:0 til 1:3.The present invention is concerned with aqueous surfactant concentrates containing 25-80% by weight of water-soluble salts of aliphatic alkoxylated and then sulfated alcohols (ether sulfate salts) together with small amounts of viscosity regulators. These surfactant concentrates are characterized in that the soin viscosity regulators contain 1-10% by weight of water-soluble alkali metal, ammonium and / or amine salts of disulfates of polyethylene glycol and / or of polypropylene glycol having a molecular weight of the polyalkylene ether glycol of 600-6000, on request. together with lower polyalkylene ether glycols having a molecular weight of 1500-6000 in a ratio of 1: 0 to 1: 3.

Til forbedring af flydeforholdet hos tungt bevægelige vandige tensidkoncentrater af vandoplosêlige salte af ikke-aromatiske 15 alkoxylerede, sulfaterede alkoholer med 8 til 24, fortrinsvis 8 til 18 carbonatomer, tilsættes ringe mængder viskositets-regulator. Ved fremgangsmâden anvender man som viskositetsre-gulator vandoplosêlige salte af disulfater af lavere polyalkylenetherglycoler med en molekylvægt pâ mindst 600, fortrinsvis 20 pâ mindst 1000. Herved kan der om onsket medanvendes de ikke sulfaterede frie, lavere polyalkylenetherglycoler med en molekylvægt pâ mindst 1500.To improve the flow ratio of heavily moving aqueous surfactant concentrates of water-soluble salts of non-aromatic 15 alkoxylated sulfated alcohols of 8 to 24, preferably 8 to 18 carbon atoms, small amounts of viscosity regulator are added. In the process, water-soluble salts of disulfates of lower polyalkylene ether glycols having a molecular weight of at least 600, preferably 20 of at least 1000, are used as viscosity regulator. If desired, the non-sulfated free, lower polyalkylene ether glycols of at least 1500 molecular weight can be used.

Af sulfaterne har især disulfaterne af lavere polyalkylen-25 etherglycoler, nemlig især af polyethylenoxid og/eller af polypropylenoxid, vist sig at være særlig virkningsfulde viskositetsregulatorer, ogsâ til hojkoncentrerede vandige tensidkoncentrater af alkylethersulfater. Den viskositetssænkende virkning eller formindskende virkning pâ gelens tykkelsesti1-30 stand af disse regulatorer tiltager med stigende molekylvægt eller stigende polykondensationsgrad af alkylenetherglycolen. Fortrinsvis andrager molekylvægten af basismaterialet til viskositetsregulatoren ca. 1000. Molekylvægte pâ indtil 6000 eller derover kan herved komme i betragtning. Særlig fore-35 trukne er disulfater af polyalkylenetherglycoler af den an- 4In particular, of the sulfates, the disulfates of lower polyalkylene ether glycols, namely, of polyethylene oxide and / or of polypropylene oxide, have been found to be particularly effective viscosity regulators, as well as to high-concentration aqueous surfactant concentrates of alkyl ether sulfates. The viscosity-lowering or reducing effect on the thickness range of the gel of these regulators increases with increasing molecular weight or increasing polycondensation degree of the alkylene ether glycol. Preferably, the molecular weight of the base material for the viscosity regulator is approx. 1000. Molecular weights of up to 6000 or more may be considered. Particularly preferred are disulfates of polyalkylene ether glycols of the present 4

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forte art med moleky1vægte i omràdet fra 1500 til 4000 eller fra 1500 til 3000. De ifolge opfindelsen som viskositetsregu-latorer benyttede disulfater hidrorer sâledes i reglen fra polyglycoler, der adskiller sig fra polyalkylenetherglycoler, 5 som - foràrsaget af ringe spor af vand - kan dannes ved oxalkyleringen af fedtalkoholer. Ifolge opfindelsen kan visko-sitetsregulatorerne anvendes pâ forudbestemt mâde i overens-stemmelse med arten og mængden deraf, sâ at tilstræbte virk-ninger, som kan forudbestemmes, er mulige i henseende til for-10 mindskelsen af gelti1standen. De ifolge opfindelsen benyttede viskositetsregulatorer er selv virkningsfulde vaskeaktive stoffer. En uonsket belastning med inaktive komponenter undgâs. Tensldblandingerne ifolge opfindelsen er ikke alene pumpbare som sâdanne i hojkoncentreret form, idet der ved for-15 tynding med vand ikke indtræder nogen stigning i geltilstan- den, men den onskede fortyndingsvirkning. Alligevel kan man efter sænkning af tensidindholdet til de i praksis onskede lavere værdier pâ eksempelvis ca. 10 til 25 vægt% ved tilsæt-ning af neutrale salte fortykke de nu i og for sig let bevæ-20 gelige flydende, vandige oplosninger.species with molecular weights in the range of 1500 to 4000 or 1500 to 3000. The disulfates used in the invention as a viscosity regulator are thus usually derived from polyglycols which differ from polyalkylene ether glycols, 5 which - caused by low traces of water - can be formed by the oxalkylation of fatty alcohols. According to the invention, the viscosity controllers can be used in a predetermined manner according to the nature and amount thereof, so that desired effects which can be predetermined are possible with respect to the reduction of the gel state. The viscosity regulators used in accordance with the invention are themselves effective detergents. An unwanted load with inactive components is avoided. The surfactant compositions of the invention are not only pumpable as such in highly concentrated form, since, when diluted with water, no increase in the gel state occurs, but the desired dilution effect. Nevertheless, after lowering the surfactant content to the practically desired lower values of e.g. 10 to 25 wt.% By the addition of neutral salts, they now thicken easily moving liquid aqueous solutions.

Onskede vandoploselige salte af de ifolge opfindelsen benyttede viskositetsregulatorer kan anvendes. Til den praktiske anvendelse kommer især alkalisalte, oploselige jordalkali-25 salte, eksempelvis magnesiumsalt, ammoniumsalt og/eller salte med organiske aminer, eksempelvis alkylolaminsalte, i be-tragtning. Det til den praktiske anvendelse vigtigste sait er natriumsaltet af disulfatet af polyethylenglycol og/eller 1,2-polypropylenglycol - med de angivne mindstemolekylvægte.Desired water-soluble salts of the viscosity regulators used in the invention can be used. For the practical application, especially alkali salts, soluble soil alkali salts, for example magnesium salt, ammonium salt and / or salts with organic amines, for example alkylolamine salts, are considered. The most important site for practical use is the sodium salt of the disulfate of polyethylene glycol and / or 1,2-polypropylene glycol - with the minimum molecular weights indicated.

3030

Viskositetsregulatorerne foreligger i de vandige tensidkon-centrater i mængder fra 1 til 10 vægt%. Serlig foretrukne kan mængder fra 2 til 5 vægt% være. I detaljer bestemmes mængden af viskositetsregulatoren ved den onskede sænkning af gelpunk-35 tet og/eller ved fortykkelsesvirkningen af det pâgældende 5The viscosity regulators are present in the aqueous surfactant concentrates in amounts from 1 to 10% by weight. Particularly preferred may be amounts from 2 to 5% by weight. In detail, the amount of viscosity regulator is determined by the desired lowering of the gel point and / or by the thickening effect of the current 5.

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alkylethersulfat. Endelig kan graden af alkoholens polyalkoxy-lering være betydningsfuld. Sâledes kan lavere alkoxylerede alkoholer ogsâ virkningsfuldt pâvirkes i heje koncentrationer, sædvanligvis med 2 til 5 vægt% af viskositetsregulatoren, 5 medens noget sterre mængder af viskositetsregulatoren kan være nodvendige i forbindelse med hejt polyalkoxylerede alkoholer (polymerisationsgrad af polyalkoxygruppen over 10 indtil ek-sempelvis 100).ether sulfate. Finally, the degree of polyalkoxylation of the alcohol may be significant. Thus, lower alkoxylated alcohols may also be effective at high concentrations, usually with 2 to 5% by weight of the viscosity regulator, while somewhat higher amounts of the viscosity regulator may be necessary in conjunction with high polyalkoxylated alcohols (degree of polymerization of the polyalkoxy group above 10). .

10 Som anfort i det foregâende kan der om onsket sammen med sul-faterne af polyethylenglycolen og/eller polypropylenglycolen anvendes fri polyethylenglycol og/eller fri polypropylenglycol som viskositetsregulerende komponenter. Ogsâ her har det vist sig, at virkningen af disse ikke sulfaterede polyalkylenether-15 glycoler pptræder desto mere udpræget, jo hojere polyalkylen-etherglycolens molekylvægt er. Disse frie polyalkylenethergly-coler, der eventuelt kan medanvendes, skal i det mindste hâve en molekylvægt pâ 1500, og fortrinsvis andrager deres molekylvægt mindst 2000 og ligger eksempelvis i omrâdet fra 2000 til 20 6000, især i omrâdet fra 3000 til 5000.As noted above, if desired, with the sulphates of the polyethylene glycol and / or polypropylene glycol, free polyethylene glycol and / or free polypropylene glycol can be used as viscosity regulating components. Here, too, it has been found that the effect of these non-sulfated polyalkylene ether glycols appears the more pronounced the higher the molecular weight of the polyalkylene-ether glycol. These free polyalkylene ether glycols, which may be used together, must have at least a molecular weight of 1500 and preferably their molecular weight at least 2000 and are, for example, in the range of 2000 to 20,000, especially in the range of 3000 to 5000.

Blandingsforholdet iaellem sulfateme af de lavere polyalky= lenetherglycoler - især disulfaterne - og de frie polyalky= lenetherglycoler ligger fordelagtigt i omrâdet fra 1:0 til 25 1:3. Blandingsomrâdet fra 1:0 til 1:1 foretrækkes i alminde- lighed.The mixing ratio between the sulfates of the lower polyalkylene ether glycols - especially the disulfates - and the free polyalkylene len ether glycols is advantageously in the range of 1: 0 to 1: 3. The mixing range from 1: 0 to 1: 1 is generally preferred.

Viskositetsregulatoren kan inden for opfindelsens rammer sættes til det vandige tensidkoncentrat som forinden dannet 30 forbindelse eller som en forinden dannet forbindelsesblanding. Herved anvendes viskositetsregulatoren hensigtsmæssigt som koncentreret vandig opl0sning (indhold af WAS fra 50 til 90%) 35 6The viscosity controller can be added within the scope of the invention to the aqueous surfactant concentrate as a pre-formed compound or as a pre-formed compound mixture. Hereby, the viscosity regulator is suitably used as concentrated aqueous solution (content of WAS from 50 to 90%).

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og blandes med den vandige oji>l0sning af alkylethersulfatet.and mixed with the aqueous solution of the alkyl ether sulfate.

I en særlig udf0relsesform for opfindelsen er det imidlertid ogsâ muligt at fremstille viskositetsregulatoren ved sulfa-tering af de lavere polyalkylenetherglycoler in situ i nær-5 værelse af den ikke-aromatiske alkoxylerede alkohol. I denne udf0relsesform bliver alkoxyleringen af sâvel de ikke-aroma-tiske alkoholer som af de forinden dannede lavere polyalkylen= etherglycoler hensigtsmæssigt foretaget i forbindelse med hin-anden. Her bliver sâledes de 0nskede blandingsforhold mellem 10 ikke-aromatisk alkohol og lavere polyalkylenetherglycol ind-stillet pâ enkel mâde, hvorefter denne stofblanding under-kastes den i og for sig kendte sulfatering. Endelig bliver de dannede sulfater omdannet til det 0nskede vandopl0selige sait. Herved bliver den samme kation indf0rt i alkylether= 15 sulfatet og i viskositetsregulatoren. I al almindelighed kan dette være en foretrukken udf0relsesform for opfindelsen.However, in a particular embodiment of the invention, it is also possible to prepare the viscosity regulator by sulfating the lower polyalkylene ether glycols in situ in the vicinity of the non-aromatic alkoxylated alcohol. In this embodiment, the alkoxylation of both the non-aromatic alcohols as well as the previously formed lower polyalkylene = ether glycols is conveniently carried out in conjunction with one another. Thus, the desired mixing ratios of 10 non-aromatic alcohol to lower polyalkylene ether glycol are adjusted in a simple manner, after which this compound is subjected to the sulfation known per se. Finally, the resulting sulfates are converted to the desired water-soluble site. Hereby the same cation is introduced into the alkyl ether = the sulfate and in the viscosity regulator. In general, this may be a preferred embodiment of the invention.

Vedr0rende den bestemte kemiske natur af alkylethersulfaterne henvises til de angivelser, der fremgâr af omtalen af teknik-kens standpunkt. Der er her principielt taie om sulfater af 20 alkoxylerede Cg-C2^-alkoholer, fortrinsvis om sâdanne deriva-ter med en carbonatomkæde pâ 8 til 18 carbonatomer. Særlig foretrukne er ikke-aromatiske alkoholer med carbonatomkæder med 10 til 16 led · Carbonatomkæden kan være ligekædet og/eller forgrenet samt mættet og/eller umættet. Alkoholer 25 af den nævnte art kan som allerede anf0rt opnâs sâvel ud fra naturprodukter som ad syntetisk vej.Regarding the specific chemical nature of the alkyl ether sulfates, reference is made to the disclosures made in the disclosure of the prior art. Here, in principle, there is much concern about sulfates of 20 alkoxylated C 9 -C 20 alcohols, preferably about such derivatives having a carbon atom chain of 8 to 18 carbon atoms. Particularly preferred are non-aromatic alcohols with 10 to 16 membered carbon atom · The carbon atom chain may be straight and / or branched as well as saturated and / or unsaturated. Alcohols 25 of the kind mentioned can, as already stated, be obtained from natural products as well as by synthetic route.

Alkoholerne er i et f0rste trin alkoxyleret med lavere alky= lenoxider. Herved kan der skelnes mellem de to store grupper af de lavt alkoxylerede og de h0jt alkoxylerede derivater.The alcohols are alkoxylated with lower alkylene oxides in the first step. Hereby the two major groups of the low alkoxylated and the high alkoxylated derivatives can be distinguished.

30 I de lavt alkoxylerede derivater er indtil 10, fortrinsvis 1 til 4, og især 2 til 3 alkoxygrupper adderet til alkohol»* gruppen. I de h0jt alkoxylerede derivater findes polyalkoxy= grupper med et ledantal over 10, eksempelvis indtil 1Q0, og især fra 20 til 80. De vigtigste alkoxyleringsmidler er ethy=In the low alkoxylated derivatives, up to 10, preferably 1 to 4, and especially 2 to 3 alkoxy groups are added to the alcohol group. In the highly alkoxylated derivatives there are polyalkoxy groups having a number greater than 10, for example up to 1Q0, and especially from 20 to 80. The most important alkoxylating agents are ethyl

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7 lenoxid og/eller 1,2-propylenoxid.7 lenoxide and / or 1,2-propylene oxide.

Som gruppe af egnede vandopl0selige salte af de sulfaterede polyalkoxylerede forbindelser egner sig den tidl&gere i for-bindelse med viskositetsregulatoren nævnte gruppe af kationer.As the group of suitable water-soluble salts of the sulfated polyalkoxylated compounds, the former group of cations mentioned in connection with the viscosity regulator is suitable.

5 Egnede salte er sâledes især alkalisaltene, opl0selige jord-alkalisalte, ammoniumsalte samt salte med organidke aminer.Suitable salts are, in particular, the alkali salts, soluble alkaline earth salts, ammonium salts and salts with organic amines.

Det i praksis vigtigste sait er natriumsaltet af ;alkylether= sulfatet.The most important site in practice is the sodium salt of; alkyl ether = the sulfate.

Foruden disse alkylethersulfatsalte kan de vandige tensidkon-10 centrater if0lge opfindelsen ogsâ indeholde andre-overflade-aktive midler. Egnede er eksempelvis ikke-ionisk.e .WAS, eksem-pelvis alkylphenolethere,Yderligere muligheder for medbenyt-tede detergenter fremgâr af den kendte teknik, der er nævnt i det foregâende.In addition to these alkyl ether sulfate salts, the aqueous surfactant concentrates of the invention may also contain other surface active agents. Suitable are, for example, nonionic, e.g., WAS, for example, alkyl phenol ethers. Further possibilities for co-used detergents are apparent from the prior art mentioned above.

15 Fra fremstillingen af alkylethersulfateterne og/eller de if01ge opfindelsen benyttede viskositetsregulatorer fore‘ligger sæd-vanligvis smâ mængder salte, sâsom natriumchlorid og/eller natriumsulfat, i de vandige koncentrater. Ogsâ her henvises til angivelserne i den refererede kendte teknik.From the preparation of the alkyl ether sulfates and / or the viscosity regulators used in the invention, usually small amounts of salts, such as sodium chloride and / or sodium sulfate, are usually present in the aqueous concentrates. Here, too, reference is made to the references in the prior art referred to.

20 Eksempler.20 Examples.

Eksempel 1.Example 1.

I en række sammenligningsfors0g bestemmes de viskositetsre-gulerende egenskaber af polyethylenglycoldisulfat og 1,2-polypropylenglycoldisulfat pâ vandige 70%'ige alkylether= 25 suifatkoncentrater. Derved konstateres den viskositetsregu- lerende virkningsafhængighed af de inest forskelLige paramétré.In a series of comparative experiments, the viscosity-regulating properties of polyethylene glycol disulfate and 1,2-polypropylene glycol disulfate are determined on aqueous 70% alkyl ether = 25 sulfate concentrates. Thus, the viscosity-regulating effect dependence of the different parameters is found.

De i dette eksempel benyttede produkter er karakteriseret som f01ger:The products used in this example are characterized as follows:

DK 156274 BDK 156274 B

8 (forkortet C12/14-2-sulfat) 70 vægt% vaskeaktivt materiale (ethanolopl0selige mængder) 0,4 vægt% NaCl 0,9 vægt% Na2S0^.8 (abbreviated C12 / 14-2 sulfate) 70% by weight detergent (ethanol soluble amounts) 0.4% by weight NaCl 0.9% by weight Na2SO4.

5 2. Na-C 12/14-fedtalkohol-3-EO-sulfat, (forkortet C12/14-3-sulfat) 70 vægt% vaskeaktivt materiale (ethanolopl0selige mængder) 0,4 vægt% NaCl 0,9 vægt% Na2S0^.2. Na-C 12/14 fatty alcohol-3-EO sulfate, (abbreviated C12 / 14-3 sulfate) 70% by weight detergent (ethanol-soluble amounts) 0.4% by weight NaCl 0.9% by weight Na2SO4 .

.10 3. Polyethylenglycoldisulfater pâ basis af polyethylenglyco= 1er med molekylvægtene 60Q, 1550, 2000 og 3000, der er op-nâet ved hjælp af direkte snlfatering med chlorsulfonsyre og foreligger soin ca. 70 vægt% vandig opl0sning..10 3. Polyethylene glycol disulfates on the basis of polyethylene glyco = 1s having molecular weights 60Q, 1550, 2000 and 3000 obtained by direct slurry fumigation with chlorosulfonic acid and available in approx. 70% by weight of aqueous solution.

4. Polypropylenglycoldisulfater pâ basis af polypropylendi= 15 glycoler med molekylvægtene 620, 1020 og 2020, der lige- ledes er fremstillet if0lge sædvanlig metode ved hjælp af direkte sulfatering af de tilsvarende polypropylenglycoler og foreligger som ca. 70% opl0sninger i vand.4. Polypropylene glycol disulfates on the basis of polypropylene = 15 glycols having molecular weights 620, 1020 and 2020, also prepared according to the usual method by direct sulfation of the corresponding polypropylene glycols and available as approx. 70% solutions in water.

a) I en f0.rste fors0gsrække konstateres viskositetens afhæng- 20 ighed (bestemt if01ge Hôppler pâ kuglefaldsviskosimeter ved 20°C) af molekylvægten af det benyttede polyethylen= glycoldisulfat. I den f01gende tabel I og i de yderligere tabeller i dette eksempel er derfor talværdierne for vis-kositeten angivet i mPas.a) In a first test series, the dependence of the viscosity (determined according to Hoppler on ball drop viscometer at 20 ° C) of the molecular weight of the polyethylene = glycol disulfate used is determined. Therefore, in the following Table I and in the additional tables in this example, the numerical values of the viscosity are given in mPas.

25 Som tensid anvendes Na"Cl2/14~fedtalkohol-2-EO'Sulfat i udgangsopl0sningen.As surfactant, Na 2 Cl 2/14 ~ fatty alcohol-2-EO'S sulfate is used in the starting solution.

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99

Tabel I.Table I.

WAS Indhold Uden til- .Molekylvægt af de grundlæggende vægt% af PGS+) sætning polyethylenglycoler'__ __vægt%___6Ôa | 1550 .2000 ~ 3000 5 70 3 150 000 120 000 60 000 SD 000 60 000 4 80 000 65 2,8 ikke 50 000 3,7 mâlelig 30 0Q0 + PGS = polyglycoldisulfat.WAS Contents Without added molecular weight of basic weight% of PGS +) statement polyethylene glycols' __ __weight% ___ 6Ôa | 1550 .2000 ~ 3000 5 70 3 150 000 120 000 60 000 SD 000 60 000 4 80 000 65 2.8 not 50 000 3.7 measurable 30 0Q0 + PGS = polyglycol disulfate.

10 b) I en næste fors0gsrække bestemmes viskositetens afhængighed af arten af det grundlæggende alkylethersulfat ved anvendelse af polypropylenglycoldisulfat (molekylvægt 15500-(B) In a further test series, the viscosity dependence of the nature of the basic alkyl ether sulfate is determined using polypropylene glycol disulfate (molecular weight 15500-

Tabel II.Table II.

15 WAS Indhold C12/14-2-sulfat C12/14-3-sülfat vægt% af PGS+ uden til- med til- uden til- med til- __vægt% sætning sætning sætning .sætning_ 70 3 150000 60000 180000 '35000 4 80000 -40000 20 65 2,8 ikke 50000 ikke >150000 3/7 ^leU-ç, 300QO mâlelig 150000 J· PGS = polyglycoldisulfat.15 WAS Content C12 / 14-2 sulphate C12 / 14-3 sulphate wt% of PGS + without addition with- without addition- with- __weight% sentence statement sentence statement. Statement_ 70 3 150000 60000 180000 '35000 4 80000 - 40000 20 65 2.8 not 50000 not> 150000 3/7 ^ leU-ç, 300QO measurable 150000 J · PGS = polyglycol disulfate.

c) I en yderligere fors0gsrække bestemmes viskositetens afhængighed af arten af polyglycolen eller af det tilsvarende 25 vandopl0selige sulfatsalt.c) In a further series of experiments, the dependence of the viscosity on the nature of the polyglycol or the corresponding water-soluble sulfate salt is determined.

Benyttet tensid: Na-C12/14-fedtalkohol-2-EO-sulfat Polyglycoldisuifat-mængde; 2„8% WAS: 65%,Surfactant used: Na-C12 / 14 fatty alcohol-2-EO-sulfate Polyglycol disulfate amount; 2 "8% WAS: 65%,

Tabel III.Table III.

1010

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Tilsætning Viskositet (mPas.)Addition Viscosity (mPas.)

Uden tilsætning ikke mâleligWithout addition not measurable

Polyethylenglycol-600-disulfat 80 000 5 " -1550- " 50 000 ” -3000- " 40 000Polyethylene Glycol 600 Disulfate 80,000 5 "-1550-" 50,000 "-3000-" 40,000

Polypropylenglycol-620-disulfat 90 000 " -1020- " 40 000 . " -2020- " 40 000 10 d) I en afsluttende fors0gsserie bestemmes genfortykke- ligheden af dialkylethersulfatopl0sninger, som blev gjort mere flydende ved hjælp af vandtilsætning.Polypropylene glycol-620-disulfate 90,000 "-1020-" 40,000. "-2020-" 40 000 10 d) In a final series of experiments, the re-thickening of dialkyl ether sulfate solutions which were made more liquid by water addition was determined.

Na-C12/14-2-sulfat g0res flydende med 3 vægt% eller 6 vægt% af viskositetsregulatoren og unders0ges i henseende til 15 dets evne til atter at blive fortykket med kogsalt efter fortynding med vand til et WAS-indhold pâ 10 vægt%. I den f01gende tabellariske sammenstilling er de if01ge opfindel-sen opnâede resultater sammenlignet med résultaterne op-nâet med tilsvarende opl0sninger, der som viskositetsregu-20 lator indeholder butylglycolsulfat eller cumensulfonat.Na-C12 / 14-2 sulfate is liquefied with 3 wt.% Or 6 wt.% Of the viscosity regulator and tested for its ability to be again thickened with boiling salt after dilution with water to a WAS content of 10 wt.%. In the following tabular composition, the results of the present invention are compared with the results obtained with similar solutions containing as a viscosity regulator butyl glycol sulphate or cumene sulphonate.

Tabel IV.Table IV.

NaCl Uden tilsætning Polyethylenglycol Butylglycol= Cumensul= (S) til at g0re fly- 1550-sulfat sulfat fonat __dende__3% 6% 3% { 6% 3% I 6% 25 3 47 47 29 33 26 14 14 5 5470 5440 6200 4030 1490 670 670 7 28170 20500 22600 18290 12380 9520 282Q0 9 14780 5230 5200 8800 8900. 9640 9600NaCl Without Addition Polyethylene Glycol Butyl Glycol = Cumensul = (S) to Make Fly 1550 Sulfate Sulfate Phonate __ ending__3% 6% 3% {6% 3% I 6% 25 3 47 47 29 33 26 14 14 5 5470 5440 6200 4030 1490 670 670 7 28170 20500 22600 18290 12380 9520 282Q0 9 14780 5230 5200 8800 8900. 9640 9600

Tabellerne vedr0rende a} og b) viser, at allerede ringe mæng-30 der af viskositetsregulatorerne if01ge opfindelsen indvirker pâ h0jkoncentrerede fedtalkoholethersulfater med hensyn til 11The tables on a} and b) show that already small amounts of the viscosity regulators of the invention affect high-concentration fatty alcohol ether sulfates with respect to 11

DK 156274 BDK 156274 B

at g0re dem mere flydende. Ved overgang til mindre koncentra-tioner, dvs. ved fortynding, forages viskositeten ikke spring-lignende, men der fremkoramer en formindskelse.to make them more fluid. When switching to smaller concentrations, ie. by dilution, the viscosity is not jump-like, but a reduction results.

I forhold til kortkædede alkylethersulfater (b.utylglycolsul= 5 fat) bliver genfortykkeligheden af de fortyndede tensidopl0s-ninger mindre pâvirket. I forstærket grad gælder dette for sammenligningen med cumensulfonat.Compared to short chain alkyl ether sulphates (butylglycol sulph = 5 barrels) the re-thickening of the diluted surfactant solutions becomes less affected. To a greater extent this applies to the comparison with cumensulfonate.

Eksempe1 2.Example1 2.

Den vandige opl0sning af et Na-C12/14-fedtalkohOl-50 EO-sul= 10 fat med et indhold af aktivt materiale pâ 25 vægt% har et gelpunkt pâ +12°C. Til formindskelse af gelpunktet anvendes dinatriumpolyethylenglycoldisulfater pâ basis af polyethylen= glycoler med molvægten 155Q, 3000 og 4000. Ved tilsætning af 1,2 vægtdele dinatriumpolyethylenglycoldisulfat til 100 vægt-15 dele fedtalkohol-EO-sulfat formindskes udgangsopl0sningens gelpiinkt til de i tabel V anf0rte værdier.The aqueous solution of a Na-C12 / 14 fatty alcohol-50 EO-sol = 10 barrels containing an active material content of 25% by weight has a gel point of + 12 ° C. To reduce the gel point, disodium polyethylene glycol disulfates on the basis of polyethylene glycols having a molecular weight of 155Q, 3000 and 4000 are used.

Tabel V.Table V.

Tilsætning Gelpunkt (°C)Addition Gel point (° C)

Uden tilsætning + 12 20 Polyethylenglycol-1550-disulfat + 2Without addition + 12 20 Polyethylene glycol-1550 disulfate + 2

Polyethylenglycol-3000~disulfat - 1Polyethylene glycol-3000 ~ disulfate - 1

Polyethylenglycol-4000-disulfat ^ 3Polyethylene glycol-4000-disulfate ^ 3

Denne fors0gsrække viser, at allerede den ringe tilsætning af 1,2 vægt%, regnet i forhold til fedtalkohol'-EO-sulfat, 25 bevirker en gelpunktsformindskelse af .st0.rrelsesordenen 10°C.This series of experiments shows that already the slight addition of 1.2% by weight, calculated in relation to fatty alcohol'-EO sulfate, causes a gel point reduction of the order of 10 ° C.

Eksempel 3.Example 3

Et tillejringsprodukt af 50 mol ethylenoxid til et mol C12/14-An adhesive product of 50 moles of ethylene oxide to one mole of C12 / 14

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12 fedtalkohol sulfateres alene samt i de i tabel VI an£0rte blandinger med polyethylenglycol under sædvanlige betingel-ser med chlorsulfonsyre. Derved anvendes 1,05 mol chlorsul= fonsyre pr. mol hydroxylgrupper (beregnet efter OH-tallet).12 fatty alcohols are sulfated alone and in the mixtures listed in Table VI with polyethylene glycol under usual conditions with chlorosulfonic acid. Thus, 1.05 moles of chlorosul = phonic acid per ml are used. moles of hydroxyl groups (calculated by OH number).

5 Efter neutralisering med natronlud og indstilling af en kon-centration af aktivt materiale pâ 25 vægt% findes de i tabel VI anfÿrte gelpunkter.5 After neutralization with baking soda and setting a concentration of active material at 25% by weight, the gel points listed in Table VI are found.

Tabel VI.Table VI.

Udgangsmateriale OH- Gelpunkt ______tal__fç_ 10 C12/14-fedtalkohol + 50 EO 25 + 12 100 vægtdele C12/14-fedtalkohol + 50 EO 29 - 3 3,9 vægtdele polyethylenglycol 4000 100 vægtdele C12/14-fedtalkohol + 50 EO 29 - 2 1,3 vægtdele polyethylenglycol 1550 15 2,6 vægtdele polyethylenglycol 5000-6000Starting material OH- Point of point ______ number__fç_ 10 C12 / 14 fatty alcohol + 50 EO 25 + 12 100 parts by weight C12 / 14 fatty alcohol + 50 EO 29 - 3 3.9 parts by weight polyethylene glycol 4000 100 parts by weight C12 / 14 fatty alcohol + 50 EO 29 - 2 1 , 3 parts by weight of polyethylene glycol 1550 15 2.6 parts by weight of polyethylene glycol 5000-6000

Claims (3)

1. Vandige tensidkoncentrater indeholdende 25-80 vægt% vand-5 oploselige salte af alifatiske alkoxylerede og derpâ sulfate-rede alkoholer (ethersulfatsalte) sammen med ronge mængder viskositetsregulatorer, kendetegnet vsed, at de soin viskositetsregulatorer indeholder 1-10 vægt% vandoplosel ige alkal imetal -, ammonium- og/eller ami nsa 1 te af diisulfater af 10 polyethylenglycol og/eller polypropylenglycol med en molekyl-vægt af polyalkylenetherglycolen pâ 600-6000, om jansket sammen med lavere polyalkylenetherglycoler med en molekylvægt pâ 1500-6000 i mængdeforhold 1:0- 1:3.1. Aqueous surfactant concentrates containing 25-80% by weight of water-soluble salts of aliphatic alkoxylated and sulfated alcohols (ether sulfate salts) together with high amounts of viscosity regulators, characterized in that the soin viscosity regulators contain 1-10% by weight of water-soluble alkaline metal -, ammonium and / or aminase 1 tea of diisulfates of 10 polyethylene glycol and / or polypropylene glycol having a molecular weight of the polyalkylene ether glycol of 600-6000, if coincident with lower polyalkylene ether glycols having a molecular weight of 1500-6000 in a ratio of 1: 0 - 1: 3. 2. Vandige tensidkoncentrater ifolge krav 1, kende tegnet ved, at molekylvægten af de til grund for den som sait foreliggende viskositetsregulator liggende polyalkylenetherglycoler ligger i intervallet 1500-4000.2. Aqueous surfactant concentrates according to claim 1, characterized in that the molecular weight of the polyalkylene ether glycols underlying the viscosity regulator present is in the range 1500-4000. 3. Vandige tensidkoncentrater ifolge krav 1 eller 2, ken detegnet ved, at viskositetsregulatorerne foreligger i mængder pâ 2-5 vægt%, og at ethersulfatsaltene fore!igger i mængder pâ 50 til 80 vægt%, begge dele regnet i forhold til vandige tensidkoncentrater. 25 30 353. Aqueous surfactant concentrates according to claim 1 or 2, characterized in that the viscosity regulators are present in amounts of 2-5% by weight and that the ether sulfate salts are present in amounts of 50 to 80% by weight, both of which are calculated relative to aqueous surfactant concentrates. 25 30 35
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DE19714043C2 (en) * 1997-04-05 2002-09-26 Cognis Deutschland Gmbh Use of glycerol sulfates as viscosity regulators for concentrated aqueous alkyl (ether) sulfate pastes
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