Search Images Maps Play YouTube News Gmail Drive More »
Sign in
Screen reader users: click this link for accessible mode. Accessible mode has the same essential features but works better with your reader.

Patents

  1. Advanced Patent Search
Publication numberUS3196174 A
Publication typeGrant
Publication dateJul 20, 1965
Filing dateMar 1, 1962
Priority dateMar 1, 1962
Publication numberUS 3196174 A, US 3196174A, US-A-3196174, US3196174 A, US3196174A
InventorsCharles A Cohen
Original AssigneeExxon Research Engineering Co
Export CitationBiBTeX, EndNote, RefMan
External Links: USPTO, USPTO Assignment, Espacenet
Perhydro bis-(isoprenyl) alkyl aryl sulfonates
US 3196174 A
Abstract  available in
Images(5)
Previous page
Next page
Claims  available in
Description  (OCR text may contain errors)

United States Patent 3,196,174 Bfi-(KSGPRENYL) ALKYL ARYL SULFONATES The present invention relates to new alkyl benzene hydrocarbons which are useful in the production of biodegradable synthetic deter ents having highly superior washing properties. Further, this invention relates to the economic preparation of these hydrocarbons from inexpensive feed stocks. More particularly, this invention relates to the preparation of these hydrocarbons by reacting an aryl substituted alkyl alkali metal compound (preferably an arylallryl lithium compound) under carefully chosen reaction conditions to obtain the selective growth of two moles of isoprene on to the aralkyl metal, hydrolyzing to obtain the corresponding allradienyl benzene and hydrogenating to remove the unsaturation and thus produce the desired allryl benzene material.

Illustrated in chemical notation the new alkyl benzene hydrocarbons of this invention may be represented by the following general formula.

wherein R is a perhydro bis (isoprenyl) alkyl radical containing ten carbon atoms comprising the structure CH QHCH -CH CH -?HCH CH but cm and Z is a two to four carbon atom alkylene group, the said alkylene group containing a single methyl group branch. The alkali metal sulfonate of these materials is represented by the following formula:

so x wherein X is an alkali metal, preferably sodium, and R and Z are as above described.

Illustrative examples of the hydrocarbon materials are:

Edd-6,174 Patented July 20, 1965 The alkali metal sulfonate salts of these alkyl benzene hydrocarbons have now been found to be highly superior to other similar type detergents known in the prior art. This is true not only with respect to the washing properties of these detergents but also with respect to their capacity to be removed in conventional sewage disposal plants. Thus, the present detergents have been found to be substantially entirely absent from the effluent from such a sewage treating, having been removed by biodegradation, adsorption, and the like. This property is an extremely important factor in preventing the foaming which has been encountered particularly in Europe in rivers and streams into which the efiluent from sewage disposal plants is discharged. It should be noted that it is surprising that both of these improvements are obtained at the same time by utilizing the present easily and cheaply prepared materials having molecular structures as above described.

It is now known that conventional alkyl benzene sulfonates commercially prepared by alkylating benzene with tetrapropylene prepared by polymerizing propylene over a phosphoric acid on Kieselguhr catalyst are particularly resistant to biological degradation by bacteria normally present in microorganism populations of activated sewage sludge (and that they are not otherwise removed by adsorption, etc.). Further it is known that severe foaming and frothing have occurred in many locations where sewage disposal plants discharge their efiluent into rivers and streams. It has now been found that the detergent materials of the type described in this invention are readily degraded biologically by the microorganisms normally present in this sludge or are otherwise removed so that when processed in a sewage plant the ellluent from said plant has little or no tendency to foam.

It has now been surprisingly discovered that by the process of the present invention substantially fully biodegradable detergents are obtained and in addition these detergents possess substantially higher detersive power than conventional sodium sulfonates of tetrapropylben zene. Thus, for example, at equal concentrations approximately twice the number of dishes can be washed with the new detergents herein described compared to a conventional tetrapropyl benzene sulfonate and brightness increases of the same order of magnitude are obtained in tests comparing the effectiveness of these detergents for soiled cotton cloth. Additionally, foaming power is ex ceptional without the use of the alkanolamides of fatty acids (foam builders) conventionally used in commercial detergents.

The present invention will be more clearly understood from a consideration of the general reaction sequence as applied to preparing one of the improved detergents of the present invention. Thus, two moles of isoprene are added to or ethyl phenyl lithium by growth reaction and the product material obtained after hydrolysis, is hydrogenated to obtain the desired saturated 2-phenyl-5,9-dimethyldecane as follows:

Alternatively, after the growth reaction the product (2) may be hydrogenated directly both to remove the Li by displacement and to saturate the double bonds.

The organolithium compounds having the general formula C H ZLi, where Z is a two to four carbon alkylene group having a single methyl branch may be prepared by the following general methods:

(1) By reaction of a suitable halogenated alkyl benzene with metallic lithium, preferably in a finely divided state and in the presence of a suitable solvent. Temperatures of below 0 C. to about 100 C. may be used depending on the nature of the halide or solvent and re action times of from one to several hours may similarly vary.

(2) By reaction of a halogenated alkyl benzene with for example a lower alkyl lithium.

(3) By reaction of an alkyl benzene with an alkyl lithium compound.

C H Z--(H) +RLi C H ZLi+RH (4) By addition of an alkyl lithium compound to an unsaturated alkyl benzene. (RH below is minus RH) (5) By metal exchange with a Grignard compound prepared from a siutable halogenated alkyl benzene.

The preparation of organolithium compounds by the methods shown above and by other means is well known in the art and is not considered as a novel aspect of this invention.

Following the preparation of the aralkyl lithium com pound this material is reacted with isoprene at pressures of from one to several hundred atmospheres, preferably one to ten atmospheres, e.g. 1 to 3 atmospheres, and at temperatures of below 0 C. to 100 C., preferably 0 C. to 50 C., e.g. 25 C. for times of 0.25-25 hours, preferably 1-12 hours, e.g. 3-4 hours. The amount of isoprene added is equal to 0.8 to 4 mols, preferably 1 to 3 mols, e.g. 2 mols of isoprene per mol of metal alkyl aryl. Thus, the desired aralkadienyl metal having e.g. two mols of isoprene added is obtained.

Following the growth reaction the product is hydrolyzed and the excess sulfuric acid into sulfate.

with water at temperautres of e.g. 0 to C. to obtain the desired alkadienyl benzene. This hydrolysis may be carried out with or without an alcohol being present. If the alcohol is used, it may be added prior to the water hydrolysis. This makes the water hydrolysis less vigorous. Suitable alcohols are methanol, ethanol, isopropanol and the like. In any case considerable heat is evolved in the preliminary hydrolysis or alcoholysis and so rather large cooling capaicty is needed.

The alkadienyl benzene is then hydrogenated by conventional means. For example, this material may be contacted with two to one hundred moles of hydrogen per mole of unsaturated compound at temperatures of 25 C. to C. and pressures of one to two thousand p.s.i.g. and in the presence of any of the hydrogenation catalysts well known to the art. Suitable catalysts are platinum, palladium and nickel, either as such or supported on a carrier. Of these the preferred catalyst is Raney nickel. Alternatively, as previously mentioned hydrogenation of the metal alkadienyl benzene compounds directly to the desired alkyl benzenes with recovery of the metal hydride for reuse can be obtained using the above described conditions. When the hydrogenation is completed, the product may be recovered by filtration from the catalyst and purified by distillation. It may be further purified prior to sulfonation by mild acid and clay treatment as disclosed in US. Patent 2,688,633.

The new alkyl benzenes may be sulfonated in known manner, e.g. by contact with an excess of concentrated sulfuric acid, oleum, ClSO I-I, sulfur trioxide, etc. The sulfonation may be carried out at temperatures up to 60 C., preferably for oleum 15 C. to 60 C., e.g. 40 C. The acid concentration is preferably at least 98%. Acid of 100% concentration and preferably oleum, containing up to e.g. 20 wt. percent S0 or higher, may be employed. With higher acid concentration, lower reaction times are required, e.g. about 3 to 4 hours with 98% acid, about 2 hours with 100% acid, and preferably 0.5 to 1 hour, e.g. 0.7 hour, with oleum. Weight ratios of sulfuric acid to hydrocarbon may range from 0.811 to 2.0: l, a 1.4:1 ratio being suitable when using 20% oleum, for example. The larger the ratio, the more inorganic sulfate will be present in the product following neutralization. In many cases, the inorganic sulfate is a desirable constituent of the finished detergent composition.

The sulfonation product mixture may be separated by layering with the addition of a limited amount of Water to remove part of the excess spent acid before neutralizing or may be neutralized directly. When neutralized, the sulfonic acids are thus converted to sulfonic acid salts The neutralization may be carried out with any base or basic-reacting inorganic or organic substance. Thus, to produce sodium sulfonates, aqueous sodium hydroxide or sodium carbonates are suitably employed. Other alkali metal, alkaline earth metal, ammonium or amine salts may be similarly produced from the corresponding basic compounds. The neutralization is generally carried out by contact with basic aqueous solution at temperatures of from 20 C. to 70 C., those between 30 C. and 50 C., e.g. 50 C., being preferred.

The present invention will be more clearly understood from a consideration of the following examples.

EXAMPLE I.SYNTHESIS OF Z-PHENYL 5,9-DIMETHYLDECANE 2-phenyl 5,9-dimethyldecane was synthesized by the following series of steps.

OCCCGCC-OOH PBra 1-bromo-3,7-dimethy1oetane 2'phenyl5,9-dimethyldecene-2 (3) 2-phenyl5,9-dhnethyldemnol-Z 2 (4) 2 phe11yl 5,9-dimethyldecene-2 W 2-phenyl-5,9-dirnethyldccane (1 1-bromo-3,7-dimethy[octane One mole (158 grns.) of 3,7-dimethyloctanol-1 (8.1. 114 C. 20 torr fi /D 1.4369) made by the hydrogenation of citronellol over Raney nickel was reacted at 5 to C. with 100 grams of PBIg followed by heating on a water bath at 70 C. for 2 hours. The mixture was then distilled rapidly at low pressure (1 mm.) to a pot temperature of 125 C. to'obtain a distillate weighing 177 gms. and a residue (P(()H) of 50 grams. T .e distillate Was extracted twice with 50 ml. portions of ice-cold 96% H 80 neutralized with NHgOH and extracted with methanol. The product was dried over K CO and distilled at reduced pressure. B.P. 4445 C. 0.4 torr. Yield 156 grams=70%.

(2) 2-pizenyl-2-hydr0xy-5,9-dimet!zylciccane 155 grams (0.7 mole) of the above bromide was Grig- (3) Z-pizenyZ-5,9-dimethyldecene-Z 136 gm. of the phenyl hydroxy decane was dehydrated by retiuxng with 500 ml. of 60 wt. percent H 59 for 4 hours. After isolation the product was distilled under vacuum using a spinning band column. BF. 148 C. 4 torr. Yield 105 gm.

(4) Z-plzenyl-S,Q-dimehtyldecmze 100 gms. of the olefin was dissolved in 200 ml. of anhydrous ethanol and hydrogenated with the aid of 1.0 gram of 5% palladium on charcoal at a pressure of 40 p.s.i.g. for 4 hours.

Distillation at 5:1 reflux ratio through a spinning band column yielded 86 grns. of product. Bl. 140-141 3.9-4.0 torr. n ZO/D 1.4813.

AnaZysfs.Found: (1:87.77, (3:87.73, H=12.27.

EXAMPLE H.2-PHENYL 6,10- DIMETHYLHENDECANE H: 12.24. tl1eor.:

(1 2,6-dimethylhendecanone-Z Pseudoionone, (2,6-dimethylhendeca 2,6,8 triene-- one) made by the condensation of citral with acetone was hydrogenated at 40 p.s.i.g. and 40 C. over a palladium on charcoal catalyst until three moles of hydrogen had been absorbed. Distillation under a spinning-band column gave a pure product showing no unsaturation by infrared spectroscopy. B.P. 118 C. 12 torr. n /1) 1.4345.

(2) Z-plzenyl 6,10-dimetlzylhendecanol-Z A Grignard reagent prepared from 173 grams bromobenzene in 500 ml. anhydrous ether and 40 grams of magnesium turnings in ml. ether was reacted With 193 grams of perhydroseudoionone at 5 C. The reaction mixture was then heated under reflux for 3 hours. The reaction products were decomposed with ice and HCl and after removing solvent, distilled under reduced pressure. B.P. C. 1.2 torr. Wt. 245 gms. n 20/D=1.4972.

(3) 2-phenyl 6,1G-dimerhylkendecene-2 The above carbinol was dehydrated by heating with 500 ml. of 60% sufuric acid at 100 C. for 4 hours. The reaction product was isolated and distilled at reduced pressure. El. 97-98" C. 0.025 torr. Wt. 211 guns. n 20/D=1.5029.

(4) Z-phenyl dJO-dimethlyhendecane The above prepared olefin was reduced at 40 p.s.i.g. over a Pd catalyst. The product was fractionated through a spinning-band column. B.P. 8788 C. 0.025 torr. Wt.=189 gins. n 20/D=1.4807.

EXAMPLE III.1-PHENY1.-2,6, 1 O-TRIMETHYL- HENDECANE This alkyl benzene was prepared in the same manner as the product of Example II, except that benzyl chloride was used instead of brorno benzene.

(1) Z-phenyl 2,6,10-zrimethylhendecane-Z The above product was prepared by reacting a Grignard consisting of 18 gm. magnesium, 73 grams benzyl chloride and 200 ml. ether with 96 grams perhydroseudoionone. The crude produce was stripped to C. (it) 1 torr. without distillation. Wt.=1.34.4 grams.

(2) 1 -phenyl 2,6,10-tri'methylhendecene-Z The crude product prepared above was dehydrated at 100 C. for 4 hours with 500 grams of 60% H 80 13.1. 108-110" C. 0.08 torr. Wt. =106.4 guns. n 20/d=1.4950.

(3) I-phenyl 2,6,IO-trimethylherzdecane The above prepared olefin diluted with 250 ml. of absolute ethanol was hydrogenated at 45 C. and 40 p.s.i.g. over 2 grams of 5% Pd on charcoal. B.P. 105-160 C. 0.07 torr. Wt. :91 gms. n 20/D==1.4872.

EXAMPLE IV.-1-PHENYL 2,5,9- TRIMETHYLDECANE This hydrocarbon is prepared in similar manner to the product of Example I from l-phenyl propanone-2 and a Grignard prepared from l-bromo 3,7-dimethyloctane.

EXAMPLE V.1-PHENYL 3,6,10- T RIM ETHYLHENDECANE This hydrocarbon is prepared in similar manner to the product of Example I from l-phenyl butanone-3 and a Grignard prepared from l-bromo 3,7-dimethyloctane.

EXAMPLE VI.-2-PHENYL 7,11-

DIMETHYLDODECANE This hydrocarbon is prepared in similar manner to the product of Example I from 3-phenyl butyraldehyde and a Grignard prepared from l-bromo 3,7-dimethy1octane.

A number of the alkyl benzenes prepared above were checked for purity by means of capillary gas chromatography. Analytical data obtained by this means are more precise than a simple carbon and hydrogen analysis. Through the use of two internal standards, namely; benzene and hexadecane, relative retention times were obtained for a number of products. Retention times under the conditions noted below were calculated on the basis of benzene equal to zero and hexadecane equal to 1.00.

7 .CAP'ILLARY GAS CHROMATOGrRAPHY Instrument Barber-Colman.

Column 150 ft. capillary.

Coating Apeizon-L.

Flash heater 213C.

Column heater 200 C.

Cell temp 215 C.

Ionization source Strontium-90.

Carrier gas Argon20 p.s.i.g.

Voltage 1250.-

Product: Retention time l-phenyl dodecane 3.75 2-phenyl dodecane 2.56 3-phenyldodecane 2.12 4-phenyldodecane 1.87 5-phenyldodecane 1.75 6-phenyldodecane 1.69 2-phenyl 5,9-dimethyldecane 1.54 2-pheny1 6,10-dimethylhendecane 2.38 l-phenyl 2,6,IO-trimethylhendecane 3.92 l-phenyl 6-cyclohexylhexane 5.55 l-phenyl 5,5,7,7-tetramethyloctane 1.94

EXAMPLE VII Fifty grams of the alkyl benzenes prepared as in the above examples were sulfonated with seventy grams of 20% oleum at a maximum temperature of 55 C. for a total contact time of one-half hour. Following neutralization with sodium hydroxide, the products Were deoiled by extraction with petroleum ether and desalted by dehydration with excess sodium carbonate from a solution in isopropyl alcohol. Evaporation to dryness under vacuum gave pure dry sulfonates.

EXAMPLE VIII A number of the sulfonates prepared above were tested in a standard dishwashing procedure at a concentration of 0.03% of pure detergent in 8 grain water at a temperature of 120 F. and compared with a standard tetrapropylbenzene sulfonate.

Product: Dishes washed Sod. sulfonate 2-phenyldodecane 16 Sod. sulfonate 2-phenyl 5,9-dimethyldecane 31 Sod. sulfonate 2 phenyl 6,10 dimethylhendecane 29 Sod. sulfonate tetrapropylbenzene 15 EXAMPLE IX Cotton detergency using standard soiled cloth was determined for a number of sulfonates in a build formulation. All products were tested at 0.15 and 0.25% at 120 F. in 8 grain water of the built formulation using the following composition.

Wt. percent Test sod. alkyl benzene sulfonate 20 Sodium tripolyphosphate 30 Tetrasodium pyrophosphate 10 Sodium metasilicate 5 Sodium carboxymethyl cellulose 1 Sodium sulfate 34 Cotton Detergency 0 Increase in Reflectance Concentration (100% Active) 1 0.03% 0.05%

Ootton-SoilType U.S. T.F. U.S. T.F.

2 Phenyldodecanc 9.8 15.2 10.6 15.7 Z-Phenyl5,9-Dimethyldecane 13.9 16.8 14.5 19.0 2-Phenyl 6,10-Dimethylhendecane 13.9 18.0 16.1 19.3 l-Phenyl 2,6,10-Tri1nethylhendecane-.- 15.5 18.8 17.0 19.4 Standard Tetrapropylbenzene 4.9 10.3 10.0 12.4

8 EXAMPLE X.-BIODEGRADATION Two types of tests were employed for determining the biodegradability of the synthetic detergents prepared according to this invention.

In an Activated Sludge Test, fifty milligrams of the detergent along with one liter of synthetic sewage was fed daily to aeration units containing approximately 2000 milligrams of activated sludge per liter. Effluent from the unit was removed daily and the residual detergent determined by means of methylene-blue and the foaming characteristics determined by blowing a fixed rate of air through a standard volume of efiluent. Details of this test have been published by I. F. Nelson et al., Developments in Industrial Microbiology Plenum Press, New York, 1961.

In a Simulated River Water test the sewage organisms were acclimated to the detergent for a period of about 2 months and then starved so that the only source of food was the synthetic detergent.

The results obtained with these tests are shown below.

ACTIVATED SLUDGE TEST 1 By Methylene-Blue Test. 2 Foam height in cm.

Sodium sulfonates of above alkylbenzenes mgm. per Liter.

SIMULATED RIVER TEST tested at 50 Percent Disappearance 2 Days on Test l 26 56 Sod. Sulf. 2-Phenyldodecane 100 100 Sod. 8111!. Example I 93 Sod. Snlf. Example II 96 95 Sod. Suit. Tctrapropylbcnzene--- 0 4 After initial acclimation. 2 By Methylene-Blue.

What is claimed is:

1. The composition of matter RZ-C H --SO H which is the sulfonation product of the compound R-ZC H and wherein R is a perhydro bis-(isoprenyl) alkyl radical having predominantly the structure OH;-(fHCH CH OH OHOHT-OH2- CH; H

and Z is a two to four carbon alkylene group, the said alkylene group containing a single methyl side chain.

2. The composition of matter RZ-C H $O M which is the sulfonation product of the compound RZC H and wherein R is a perhydro bis-(isoprenyl) alkyl radical having predominantly the structure CH ([3HCH -GH -CH -CH-OHg-OH;

CH3 H3 Z is a two to four carbon alkylene group, the said alkylene group containing a single methyl side chain, and M is an alkali metal.

3. The composition of matter 9 10 which is the sulfonation product of the compound References Iited by the Examiner CH3 ?H CH2 CHFGHF$H CH2 CH2%H C6H5 UNITED STATES PATENTS CH8 3 3 1,934,123 11/33 Hofman et al 260-668 wherein M is an alkali metal. 5 2,467,170 4/49 Weinmayr 260-505 4. The composition of matter 2,517,720 8/50 Schaad 260-505 OH;CH-CH CH -CH:GHOH CH CH OH-C H;SO M 9 5 5/ 61 F055 26O668 H H 3,009,972 11/61 Johnson 260-505 a 3 3,115,530 12/63 Cohen 260-505 which is the sulfonation product of the compound 10 CH -C[HCH GH UH;:CHGH CH CH CH-C H OTHER REFERENCES OH; 0H H3 Bauzngartner: Ind. and Eng. Chem, vol. 46, 1954, wherein M is an alkali metal. 1349 1352' The Composition of matter 15 Hammenton: J. Appl. Chem, vol. 5, 1955, pp. 517-524. CH -CH-CH CH -CH -CH-CH -CH -CE -CH-CH -C611;S03M References Cited by the Applicant H3 H H3 Gray et al.: Journal of Organic Chemistry, vol. 26, which is the sulfonation product of the compound 209 19 1 CH CH-CH CH CH UHF-CH CH CH2OH=CH C H5 3- H 2 F ii H CH r LORRAINE A. WEINBERGER, Primary Examiner.

wherein M is an alkali metal. LEON ZITVER Examiner

Patent Citations
Cited PatentFiling datePublication dateApplicantTitle
US1934123 *Jul 8, 1929Nov 7, 1933Ig Farbenindustrie AgProcess for the manufacture of condensation products from diolefines and hydrocarbons
US2467170 *Oct 15, 1947Apr 12, 1949Du PontAlkyl substituted aromatic sulfonates
US2517720 *Dec 22, 1947Aug 8, 1950Universal Oil Prod CoMethod of producing propylene polymers and surface active agents derived from said polymers
US2984691 *Sep 30, 1954May 16, 1961Standard Oil CoTelomerization process
US3009972 *Sep 25, 1959Nov 21, 1961Monsanto ChemicalsDimerization of olefins
US3115530 *May 13, 1960Dec 24, 1963Exxon Research Engineering CoPreferred alkyl aryl sulfonate detergents
Referenced by
Citing PatentFiling datePublication dateApplicantTitle
US3355484 *Aug 20, 1964Nov 28, 1967Universal Oil Prod CoProcess for making biodegradable detergents
US3442964 *Jan 12, 1965May 6, 1969British Hydrocarbon Chem LtdProduction of detergent alkylate
US6274540Jan 7, 2000Aug 14, 2001The Procter & Gamble CompanyDetergent compositions containing mixtures of crystallinity-disrupted surfactants
US6303556Dec 15, 1999Oct 16, 2001The Procter & Gamble CompanyHard surface cleaning compositions comprising modified alkybenzene sulfonates
US6342473Dec 15, 1999Jan 29, 2002The Procter & Gamble CompanyHard surface cleaning compositions comprising modified alkylbenzene sulfonates
US6498134Dec 15, 1999Dec 24, 2002The Procter & Gamble CompanyDishwashing compositions containing alkylbenzenesulfonate surfactants
US6514926Oct 13, 1999Feb 4, 2003The Procter & Gamble CompanyLaundry detergents comprising modified alkylbenzene sulfonates
US6525233Jan 7, 2000Feb 25, 2003The Procter & Gamble CompanyProcess for preparing a modified alkylaryl
US6566319Jan 7, 2000May 20, 2003The Procter & Gamble CompanyCleaning products comprising improved alkylarylsulfonate surfactants prepared via vinylidene olefins and processes for preparation thereof
US6583096Oct 13, 1999Jun 24, 2003The Procter & Gamble CompanyLaundry detergents comprising modified alkylbenzene sulfonates
US6593285Jan 7, 2000Jul 15, 2003The Procter & Gamble CompanyAlkylbenzenesulfonate surfactants
US6602840Jan 7, 2000Aug 5, 2003The Procter & Gamble CompanyProcesses for making alkylbenzenesulfonate surfactants and products thereof
US6774099Dec 15, 1999Aug 10, 2004The Procter & Gamble CompanyDishwashing detergent compositions containing mixtures or crystallinity-disrupted surfactants
US6908894Oct 22, 2001Jun 21, 2005The Procter & Gamble CompanyAlkylaromatic hydrocarbon compositions
US7202205Sep 1, 1999Apr 10, 2007Daniel Stedman ConnorProcesses for making surfactants via adsorptive separation and products thereof
US9193935Dec 23, 2011Nov 24, 2015Givaudan S.A.Compounds capable of releasing fragrant compounds
US20020103096 *Oct 22, 2001Aug 1, 2002Kott Kevin LeeAlkylaryls
WO1999005242A1 *Jul 20, 1998Feb 4, 1999The Procter & Gamble CompanyImproved alkylbenzenesulfonate surfactants
WO1999005243A1 *Jul 20, 1998Feb 4, 1999The Procter & Gamble CompanyDetergent compositions containing mixtures of crystallinity-disrupted surfactants
WO1999005244A1 *Jul 20, 1998Feb 4, 1999The Procter & Gamble CompanyImproved alkyl aryl sulfonate surfactants
Classifications
U.S. Classification562/91, 260/665.00R, 510/495, 510/357, 510/235, 585/319, 585/455, 568/715, 585/254
International ClassificationC07C45/62, C07C309/31
Cooperative ClassificationC07C309/31, C07C45/62
European ClassificationC07C45/62, C07C309/31