US3753968A - Selective reaction of fatty acids and their separation - Google Patents

Selective reaction of fatty acids and their separation Download PDF

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US3753968A
US3753968A US00159070A US3753968DA US3753968A US 3753968 A US3753968 A US 3753968A US 00159070 A US00159070 A US 00159070A US 3753968D A US3753968D A US 3753968DA US 3753968 A US3753968 A US 3753968A
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acid
fatty acids
fatty
dicarboxylic acid
acids
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B Ward
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    • C—CHEMISTRY; METALLURGY
    • C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11C—FATTY ACIDS FROM FATS, OILS OR WAXES; CANDLES; FATS, OILS OR FATTY ACIDS BY CHEMICAL MODIFICATION OF FATS, OILS, OR FATTY ACIDS OBTAINED THEREFROM
    • C11C3/00—Fats, oils, or fatty acids by chemical modification of fats, oils, or fatty acids obtained therefrom
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C57/00—Unsaturated compounds having carboxyl groups bound to acyclic carbon atoms
    • C07C57/26—Unsaturated compounds having carboxyl groups bound to acyclic carbon atoms containing rings other than six-membered aromatic rings

Definitions

  • a process for making a dicarboxylic acid having 21 carbon atoms from fatty acids is accomplished by reacting the linoleic acid portion in a fatty acid mixture with up to 26% by weight of fatty acids of acrylic acid and with from 0.01% to 0.5% by weight of fatty acids of iodine catalyst at a temperature between 200 C. and 270 C.
  • the fatty acid-dicarboxylic acid mixture is then separated by distilling into an oleic-type fatty acid and a C dicarboxylic acid. This process is especially applicable to separating tall oil fatty acids.
  • This invention relates to the production of a dicarboxylic acid having 21 carbon atoms. It also relates to a process for the separation of fatty acids. More specifically, this invention relates to a process for making dicarboxylic acid having 21 carbon atoms from tall oil derived linoleic acid. As used herein the term dicarboxylic acid is intended to mean a dicarboxylic acid having 21 carbon atoms, but in some instances includes minor amounts of dicarboxylic acid or other molecular weights.
  • the invention outlined below is to be distinguished from treatment of tall oil fatty acids with iodine as set forth in US. Pat. 3,157,629 to P. D. Patrick.
  • tall oil fatty acids are heated Within a range of 450550 F. (232 C.288 C.) in the presence of an iodine catalyst until the linoleic acid portion of the fatty acid is reduced below 15%, forming saturated acids, primarily oleic acid and 2-25% dimerized acids.
  • the linoleic acid is not converted to oleic acid.
  • the process of this invention is also to be distinguished from US. Pats.
  • the tall oil starting material contains a relatively large proportion of rosin acids and is subjected to heat in the presence of a catalyst, whereupon hydrogen is generated largely from the rosin acids and serves to hydrogenate certain rosin acids as well as the unsaturated fatty acids.
  • the reactions above do not accomplish the results of this invention.
  • dicarboxylic acids are well known in the prior art as dicarboxylic acids are useful as plasticisers in the manufacture of alkyd resins and as curing agents for epoxy resins.
  • a process for making dicarboxylic acid from fatty-type acids is disclosed in British Pat. No. 1,032,363, wherein conjugated fatty acids are isomerized to a trans/trans form with iodine and subsequently reacted with a reactive dienophile to form the Diels-Alder adduct.
  • the disclosed reaction has heretofore not been applied to fatty acids containing non-conjugated linoleic acid wherein the non-conjugated linoleic acid is converted to dicarboxylic acid.
  • tall oil fatty acids containing both nonconjugated and conjugated linoleic acid are reacted with acrylic acid in the presence of catalytic amounts of iodine.
  • the acrylic acid is added to the fatty acid mixture in an amount up to about 12% by weight of fatty acids.
  • the catalytic amounts of iodine used is from 0.01% to 0.50% based on the weight of fatty acids, preferably 0.05% 0.2% by weight. The upper amount gives rapid reaction without unnecessary loss of color. If large percentages of iodine are used, i.e., above 0.5%, or if the reaction temperature is increased above 270 C.
  • oil fatty acids may be separated into two fractions by The time required for maximum conversion of linoleic distillation.
  • a 5% acid to dicarboxylic acid depends on temperature and heads cut is taken and then, one gets 50% of the feed as catalyst level.
  • the remaining 45% is dicarboxylic acid which temperature is 250 C. and 0.15% iodine is used about can be further purified, if desired, by molecular distilla- 45 minutes is required for complete conversion of the tion.
  • Using the fractional distillation method of purificalinoleic acid in the tall 011 to dicarboxylic acid is used.
  • the gas tion, a distillate which is very similar to oleic acid is obchromatography data. shows that only the linoleic acid is tained. This product is about 75% C monounsaturated reacting (percentage decreasing). There is very little fatty acids, has an acid number of 195, has only 3% diene, change in the fatty acids present in the tall oil except for and has a titer of about C. the reaction of the linoleic acid, thus, one obtains a mix-
  • the crude dicarboxylic acid material which accounts ture of tall oil fatty acid (virtually linoleic free) and the for 45% of the total, is about 92% dioarboxylic acid. dicarboxylic acid.
  • the impurities are about 5% fatty acids and 5% dimer- EXAMPLE 2 type fatty ac ds- T1118 mammal 15 Father dark smfie 1t 13 a
  • This example illustrates separation and characterization bottoms product and must be purified to get a high grade of C21 dicarboxylic acid
  • the acid mixture fro th dicarboxylic acid.
  • the C dicarboxylic acid from linoleic action of distilled tau n fan acids iodine acvid with two acid g oups is shown below.
  • a process for the production of a dicarboxylic acid from a fatty acid mixture containing conjugated linoleic acid non-conjugated linoleic acid comprising, simultaneously reacting both the non-conjugated and conjugated linoleic acid portion of the fatty acid mixture with up to 26% by weight of said fatty acids of acrylic acid and 0.01% to 0.50% by Weight of fatty acid mixture of iodine at a temperature between 200 C. and 270 C. to convert the conjugated and non-conjugated linoleic acid portion to a dicarboxylic acid having the formula wherein one X is hydrogen and the other X is a carboxylic acid group.
  • VIVIAN GARNER Primary Examiner US. Cl. X.R.

Abstract

A PROCESS FOR MAKING A DICARBOXYLIC ACID HAVING 21 CARBON ATOMS FROM FATTY ACIDS IS ACCOMPLISHED BY REACTING THE LINOLEIC ACID PORTION IN A FATTY ACID MIXTURE WITH UP TO 26% BY WEIGHT OF FATTY ACIDS OF ACRYLIC ACID AND WITH FROM 0.01% TO 0.5% BY WEIGHT OF FATTY ACIDS OF IODINE CATALYST AT A TEMPERATURE BETWEEN 200*C. AND 270*C. THE FATTY ACID-DICAROXYLIC ACID MIXTURE IS THEN SEPARATED BY DISTILLING INTO AN OLEIC-TYPE FATTY ACID AND A G21 DICARBOXYLIC ACID. THIS PROCESS IS ESPECIALLY APPLICABLE TO SEPARATING TALL OIL FATTY ACIDS.

Description

United States Patent O 3,753,968 SELECTIVE REACTION OF FATTY ACIDS AND THEIR SEPARATION Benjamin F. Ward, Charleston, S.C., assignor to Westvaco Corporation, New York, N.Y. No Drawing. Filed July 1, 1971, Ser. No. 159,070 Int. Cl. C09F N04 US. Cl. 26097.6 4 Claims ABSTRACT OF THE DISCLOSURE A process for making a dicarboxylic acid having 21 carbon atoms from fatty acids is accomplished by reacting the linoleic acid portion in a fatty acid mixture with up to 26% by weight of fatty acids of acrylic acid and with from 0.01% to 0.5% by weight of fatty acids of iodine catalyst at a temperature between 200 C. and 270 C. The fatty acid-dicarboxylic acid mixture is then separated by distilling into an oleic-type fatty acid and a C dicarboxylic acid. This process is especially applicable to separating tall oil fatty acids.
BACKGROUND OF THE INVENTION This invention relates to the production of a dicarboxylic acid having 21 carbon atoms. It also relates to a process for the separation of fatty acids. More specifically, this invention relates to a process for making dicarboxylic acid having 21 carbon atoms from tall oil derived linoleic acid. As used herein the term dicarboxylic acid is intended to mean a dicarboxylic acid having 21 carbon atoms, but in some instances includes minor amounts of dicarboxylic acid or other molecular weights.
The invention outlined below is to be distinguished from treatment of tall oil fatty acids with iodine as set forth in US. Pat. 3,157,629 to P. D. Patrick. In the Patrick process, tall oil fatty acids are heated Within a range of 450550 F. (232 C.288 C.) in the presence of an iodine catalyst until the linoleic acid portion of the fatty acid is reduced below 15%, forming saturated acids, primarily oleic acid and 2-25% dimerized acids. -In contrast, in the process of this invention, the linoleic acid is not converted to oleic acid. The process of this invention is also to be distinguished from US. Pats. 2,617,- 792 to Floyd, and 2,811,386 to Hasselstrorn. In these processes, the tall oil starting material contains a relatively large proportion of rosin acids and is subjected to heat in the presence of a catalyst, whereupon hydrogen is generated largely from the rosin acids and serves to hydrogenate certain rosin acids as well as the unsaturated fatty acids. The reactions above do not accomplish the results of this invention.
The use of dicarboxylic acids is well known in the prior art as dicarboxylic acids are useful as plasticisers in the manufacture of alkyd resins and as curing agents for epoxy resins. A process for making dicarboxylic acid from fatty-type acids is disclosed in British Pat. No. 1,032,363, wherein conjugated fatty acids are isomerized to a trans/trans form with iodine and subsequently reacted with a reactive dienophile to form the Diels-Alder adduct. However, the disclosed reaction has heretofore not been applied to fatty acids containing non-conjugated linoleic acid wherein the non-conjugated linoleic acid is converted to dicarboxylic acid.
It is therefore a general object of this invention to provide a process for making dicarboxylic acid from all of the available linoleic acid in a fatty acid mixture. Another object of this invention is to provide a process whereby tall oil fatty acids may easily be separated into a dicarboxylic acid portion and an oleic acid-type portion.
Other objects, features and advantages will be evident from the following disclosure.
Patented Aug. 21, 1973 It has been found that if a fatty acid mixture containing a significant portion of linoleic acid is treated with up to 26% by weight of fatty acids of acrylic acid and from 0.01% to 0.50% by weight of fatty acids of iodine at a temperature between 200 C. and 270 C., the linoleic acid portion of the fatty acid mixture is converted to dicarboxylic acid. Thus when the fatty acid mixture is a tall oil fatty acid mixture, and stabilized glacial acrylic acid, and iodine catalyst are heated together at 230 C.- 250 C. for about one to two hours, they produce a dicarboxylic acid along with the residual monounsaturated and saturated fatty acids. Upon distillation, a high grade oleic acid is obtained; the residue being dicarboxylic acid. Such separation of the oleic and linoleic acids in tall oil is not possible by fractional distillation of the fatty acids prior to reaction with acrylic acid.
DETAILED DESCRIPTION OF THE INVENTION There is provided by this invention a convenient process for upgrading crude and distilled fatty acids by forming different acids from one portion of the fatty acid and separating the fatty acids into distinct major fractions. Until this invention, it has been difficult to fractionally distille tall oil fatty acids into component acids because of their close boiling points. The invention is based on conversion of the total diene portion of fatty acids to dicarboxylic acid, which has a significantly higher boiling point than oleic acid.
Accordingly, tall oil fatty acids containing both nonconjugated and conjugated linoleic acid are reacted with acrylic acid in the presence of catalytic amounts of iodine. The acrylic acid is added to the fatty acid mixture in an amount up to about 12% by weight of fatty acids. The catalytic amounts of iodine used is from 0.01% to 0.50% based on the weight of fatty acids, preferably 0.05% 0.2% by weight. The upper amount gives rapid reaction without unnecessary loss of color. If large percentages of iodine are used, i.e., above 0.5%, or if the reaction temperature is increased above 270 C. a portion of the linoleic acid is converted to oleic acid and the yield of dicarboxylic acid is thereby decreased. There is a lower limit of feasibility too, for at just slightly milder reaction conditions the rate drops to almost zero. In order to maintain the highest possible yield of dicarboxylic acid from a mixed fatty acid, conditions close to the lower catalyst level and lower temperature are maintained. Selection of the ideal amount of catalyst will depend on the equipment, temperature and time of the reaction. The reaction to produce dicarboxylic acid is carried out at a temperature between 200 C. and 270 C., preferably 230 C.250 C. The reaction time at these temperatures and under the preferred catalyst level is about one to two hours.
The following is typical of the general procedure which may be used in carrying out the process of this invention on tall oil fatty acids.
To tall oil fatty acids is added up to 12% by weight of fatty acids of glacial acrylic acid and 0.1% by weight of fatty acids of iodine, at a temperature between 230 to 25 0 C. The acrylic acid catalyzed by iodine readily undergoes reaction with the fatty acids. Therefore, when tall oil fatty acids, acrylic acid and iodine are mixed together and heated to 250 C., the linoleic acid in the fatty acids is converted to dicarboxylic acid. In addition to the advantage of having a one step reaction in this case, it seems that the iodine catalyzes the addition reaction to get a very clean, rapid reaction. This one step process greatly improves the overall yield of dicarboxylic acid from fatty acids containing linoleic acid because all of the linoleic acid is immediately converted to dicarboxylic acid. The
amount of dicarboxylic acid formed is approximately the same as the starting content of linoleic in the fatty acid mixture. This process is equally applicable to fatty acids derived from sources other than tall oil, such as animal derived and vegetable derived fatty acid mixtures contain tions A-D in Table I. As can be seen, the reaction occurs at 205 C., but for optimum utility and maximum yield of dicarboxylic acid Within a reasonable time a temperature of about 250 C. is preferred. Reactions E-H show the effect of various catalyst levels and again a variety of ing substantial amounts of linoleic acid. addition levels will promote the reaction but these results One of the major advantages of this process is that tall are shown with 0.075% to 0.15% iodine. oil fatty acids may be separated into two fractions by The time required for maximum conversion of linoleic distillation. In a fractional laboratory distillation a 5% acid to dicarboxylic acid depends on temperature and heads cut is taken and then, one gets 50% of the feed as catalyst level. As is demonstrated in reactions H-J, if the distillate. The remaining 45% is dicarboxylic acid which temperature is 250 C. and 0.15% iodine is used about can be further purified, if desired, by molecular distilla- 45 minutes is required for complete conversion of the tion. Using the fractional distillation method of purificalinoleic acid in the tall 011 to dicarboxylic acid. The gas tion, a distillate which is very similar to oleic acid is obchromatography data. shows that only the linoleic acid is tained. This product is about 75% C monounsaturated reacting (percentage decreasing). There is very little fatty acids, has an acid number of 195, has only 3% diene, change in the fatty acids present in the tall oil except for and has a titer of about C. the reaction of the linoleic acid, thus, one obtains a mix- The crude dicarboxylic acid material, which accounts ture of tall oil fatty acid (virtually linoleic free) and the for 45% of the total, is about 92% dioarboxylic acid. dicarboxylic acid.
TABLE I [Variations in reaction conditions for reaction of distilled tall oil fatty acids with acrylic acid] Untreated Reaction number fatty acid A B C D E F G H I .r
A. Conditions:
Temperature, C 205 219 232 252 250 250 250 250 250 250 P entmdine 0.06 0. 6 7 0. 6 0.075 0.1 0.125 0.15 0,15 115 Time, hrs 2 a 2. 5 2. 5 2 1. 2 1 0. 5 0. 75
B. Analysis by GLC assignment:
Saturated fatty acid 5.1 6.1 0 4.3 4. 6 4. 6 4.6 4.1 5.3 5 6 01s monounsaturated fatty acid 45. 0 45. 7 47.2 46.6 45.0 44. 5 44. 9 44. 4 44. 8 44. 5 45. 0
Linoleic acid 41.4 -8 2 5 6.3 2.4 2.0 1. 4 5,4 0, 6
Other fatty acids 8.6 11.8 10.0 9.8 10.2 10.7 9.1 9.0 10.7 8.3 as
C21 dicarboxylic acid acid 0.0 12.0 20.0 24.0 35.0 34.0 39.0 40.0 40.0 30.0 42.0
The impurities are about 5% fatty acids and 5% dimer- EXAMPLE 2 type fatty ac ds- T1118 mammal 15 Father dark smfie 1t 13 a This example illustrates separation and characterization bottoms product and must be purified to get a high grade of C21 dicarboxylic acid The acid mixture fro th dicarboxylic acid. The C dicarboxylic acid from linoleic action of distilled tau n fan acids iodine acvid with two acid g oups is shown below. The theoretical acid can be Separated into i fractions fr i acid numbe is 316 and that of the Crude dicarboxyhc 4O distillation in a short path still with an inch of las s liez i s a asd isesagfiuf 308 due t0 the lmPuntms hsted above whlch in it to serve as plates. From this drsullatron a 4% heads a P fraction (100% fatty acids); 50% distillate fraction /OH=CH (97.2% fatty acids, 2.8% dicarboxylic acid); and
CH;(CH2)5GH oH-(cHz)7-ci-011 residue fraction (4.7% fatty acids, 92.1% dicarboxylie 45 acid, and 3.2% other) was obtained. The analysis of I each fraction was by gas chromatography. The other" X X portion of the residue fraction represents unidentified mawherein one X is a hydrogen (H) and the other X is a renal which does not come out in the dicarboxylic acid carboxylic acid group (COOH). peak. Most of this other material is a dimer fatty acid.
Another means, other than molecular distillation, for For the sample reported above the residue had an acid purifying the crude dicarboxylic acid is by distillation of number of 300, a saponification number of 304, a Gardner its methyl or dimethyl ester. At 0.2 mm. vacuum the (11- color of 16, and a Gardner viscosity of more than Z-6. carboxylic acid boils at 265 C., the monomethyl ester The residual dicarboxylic acid fraction was distilled at boils at 240 C., and the dimethyl ester boils at 220 C. 270 C. at 0.2 mm. to obtain a somewhat purer dicar- Therefore, by converting the crude dicarboxylic acid to its boxylic acid. However, at these high temperatures (300 dimethyl ester and then distilling, a very pure product C. pot temperature) decomposition of the dicarboxylic can be obtained. The separation from dimer acid is very acid began to occur. One of the ways for purifying the good too, since the dimethyl ester of any dimer and dicarboxylic acid is to convert it to its dimethyl ester present boils at least above about 260 The dimethyl and then distill this. The competitive distillation temester and the monomethyl ester of the dicarboxylic acid peratures of various esters are reported in Table 11.
are readily purified by fractlonal distillation; whereas the TABLE H fi fhcarboxyhc acid 15 best separated by molecular dis- [Distillation temperatures for materials in the dlcarboxylic acid 11111311011. system] The practice of this invention may clearly be seen in P 0t Vapor the following examples. ppu m 0.) C (inm.) EXAMPLE 1 Fatty acid monomer. 200 190 D. 2
To illustrate the production of C dlCfifbOXYll? acid, gggg g ggfig- '33? 54% 3:3 a series of reaction involving the addition of acrylic acid Monornethylester oidicarboxyllc acid- 205 240 0.2 to tall oil fatty acids were run. The reaction conditions g$ggffff 558 8:; and results are shown in Table I.
In these reactions 12% by Weight f the fa ty a ds Of As is illustrated by the results in Table II, by preparing glacial acrylic acid was added to the linoleic acid portion the dimethyl ester of dicarboxylic acid and purifying it of distilled tall oil fatty acids in the presence of an iodine by distillation, the fatty acid monomer and the dimer acids catalyst. The effect of temperature is illustrated by reaccan be cleanly removed. In a sample treated in this manner and then reacidified, the gas chromatograph showed the sample to be 93% dicarboxylic acid. It has an acid number of 310.
While the invention has been described and illustrated herein by references to various specific materials, procedures and examples, it is understood that the invention is not restricted to the particular materials, combinations of materials, and procedures selected for that purpose. Numerous variations of such details can be employed, as will be appreciated by those skilled in the art.
What is claimed is:
1. A process for the production of a dicarboxylic acid from a fatty acid mixture containing conjugated linoleic acid non-conjugated linoleic acid comprising, simultaneously reacting both the non-conjugated and conjugated linoleic acid portion of the fatty acid mixture with up to 26% by weight of said fatty acids of acrylic acid and 0.01% to 0.50% by Weight of fatty acid mixture of iodine at a temperature between 200 C. and 270 C. to convert the conjugated and non-conjugated linoleic acid portion to a dicarboxylic acid having the formula wherein one X is hydrogen and the other X is a carboxylic acid group.
2. The process of claim 1 wherein said fatty acid mixture is a tall oil fatty acid mixture.
3. The process of claim 1 wherein said iodine is present at 0.05 to 0.20% by weight and said temperature is between 230 C. and 250 C.
4. The process of claim 1 further comprising, distilling the fatty acid mixture containing dicarboxylic acid and recovering a linoleic free fatty acid fraction and a dicarboxylic acid fraction.
References Cited FOREIGN PATENTS 1,032,363 6/1966 Great Britain 26097.5
VIVIAN GARNER, Primary Examiner US. Cl. X.R.
2 2 3 UNETED STATES PATENT OFFICE QERTEFECATE 6F CORRECTIQN Patent No. 3,7 3, 8 Dated August 21 1973 l Benjamin F. ward It is certified that error appears in the above-identified patent and that said Letters Patent are hereby corrected as shown below:
Co1umn I line 33, ""or" should read of Co1um'n 3, Hne 69, "reaction" should read react1'ons a i.-
Claim 1, line 3, "acid", first occurrence, should read and CH=CH 0 -u Glam 1, the formula should read- CH CH -CH CH-(CH -C-0H CH-CH i I l X Signed and sealed this 26th day of March 1974.
(SEAL) Attest:
EDWARD M.FLETCHER,JR. C. MARSHALL DANN Attesting Officer Commissioner of Patents
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DE102007053953A1 (en) 2007-11-09 2009-05-14 Henkel Ag & Co. Kgaa Styling agent with high moisture retention III
DE102007053955A1 (en) 2007-11-09 2009-05-14 Henkel Ag & Co. Kgaa Styling agent with high retention in moisture II
DE102007053957A1 (en) 2007-11-09 2009-05-14 Henkel Ag & Co. Kgaa Styling agent with a high degree of hold on wetness IV
DE102007053952A1 (en) 2007-11-09 2009-05-14 Henkel Ag & Co. Kgaa Agent containing ester compound with wax alcohol component
US20100215609A1 (en) * 2007-11-09 2010-08-26 Thorsten Knappe Styling Agents Giving a High Degree of Hold in Humid Conditions
DE102007053951A1 (en) 2007-11-09 2009-05-14 Henkel Ag & Co. Kgaa Styling agent with a high degree of hold in humidity
DE102007053950A1 (en) 2007-11-09 2009-05-14 Henkel Ag & Co. Kgaa Agent with bioflavonoid
DE102007053954A1 (en) 2007-11-09 2009-05-14 Henkel Ag & Co. Kgaa High-retention styling agent with moisture V
US8398960B2 (en) 2007-11-09 2013-03-19 Henkel Ag & Co. Kgaa Styling agents giving a high degree of hold in humid conditions
DE102007056935A1 (en) 2007-11-23 2009-05-28 Henkel Ag & Co. Kgaa Two-component aerosol hair color
EP2062616A1 (en) 2007-11-23 2009-05-27 Henkel AG & Co. KGaA Dual component aerosol hair dye
DE102009009004A1 (en) 2008-02-18 2009-09-17 Seaquist Perfect Dispensing Gmbh Dispensing device, preferably pump preferably with a sprayable and/or non-sprayable cosmetic liquid, where the cosmetic liquid comprises single phase solution, mixture of non-miscible liquid phases, and oil-in-water-/water-in-oil-emulsion
DE102008030660A1 (en) 2008-07-01 2010-01-07 Henkel Ag & Co. Kgaa Agent for keratin-containing fibers containing at least one specific cellulose and at least one additional film-forming and / or setting polymer
DE102008030661A1 (en) 2008-07-01 2010-01-07 Henkel Ag & Co. Kgaa Keratin-containing fibers containing at least one specific betaine compound and at least one film-forming and / or setting polymer
DE102008033106A1 (en) 2008-07-15 2010-01-21 Henkel Ag & Co. Kgaa Non-weighty hair treatment product with structuring effects
US8329152B2 (en) 2008-07-21 2012-12-11 Henkel Ag & Co. Kgaa Smooth styling agents
US20110110878A1 (en) * 2008-07-21 2011-05-12 Thorsten Knappe Smooth Styling Agents
DE102008035597A1 (en) 2008-07-21 2010-04-29 Henkel Ag & Co. Kgaa Styling agent with a high degree of hold and care I
DE102008034102A1 (en) 2008-07-21 2010-01-28 Henkel Ag & Co. Kgaa Supple styling agent with a high degree of hold
DE102008035598A1 (en) 2008-07-21 2010-01-28 Henkel Ag & Co. Kgaa Styling agent with a high degree of hold and care II
DE102008036952A1 (en) 2008-08-08 2009-06-10 Henkel Ag & Co. Kgaa Lightening material for keratin fibres, especially for bleaching human hair, comprises two separate components, one with hydrogen peroxide, plus an indicator which changes color when the components are mixed
DE102008038138A1 (en) 2008-08-18 2010-02-25 Henkel Ag & Co. Kgaa Agent, useful for coloring keratin fibers, which are fur, wool or feathers, preferably human hair, comprises a dye starting product and a browning product, where the browning product is obtained by heating sugar
DE102008038109A1 (en) 2008-08-18 2010-02-25 Henkel Ag & Co. Kgaa Agent, useful e.g. to treat keratin fibers, especially human hair, comprises amphiphilic, cationic polymer comprising e.g. pyrrolidin-2-one unit, and amine unit, and film-forming cationic and/or solid cationic polymer in a carrier
US9211425B2 (en) 2008-08-18 2015-12-15 Henkel Ag & Co. Kgaa Product for keratin-containing fibers comprising at least one specific amphiphilic cationic polymer, and at least one specific amphiphilic anionic polymer
US9034307B2 (en) 2008-08-18 2015-05-19 Henkel Ag & Co. Kgaa Agent for fibers containing keratin, containing at least one specific amphiphilic cationic polymer and at least one additional film-forming cationic and/or stabilizing polymer
DE102008038105A1 (en) 2008-08-18 2010-02-25 Henkel Ag & Co. Kgaa Agent for keratin-containing fibers containing at least one specific amphiphilic, cationic polymer and at least one specific amphiphilic, anionic polymer
US8685377B2 (en) 2008-08-18 2014-04-01 Henkel Ag & Co. Kgaa Agent for fibers containing keratin, comprising at least one specific amphiphilic cationic polymer and at least one specific, additional film-forming anionic and/or stabilizing anionic polymer
US8663605B2 (en) 2008-08-18 2014-03-04 Henkel Ag & Co. Kgaa Agent for fibers containing keratin, comprising at least one specific amphiphilic cationic polymer, at least one cationic styling polymer that is different therefrom and at least one film-forming non-ionic and/or stabilizing non-ionic polymer
US8506941B2 (en) 2008-08-18 2013-08-13 Henkel Ag&Co. Kgaa Agent for fibers containing keratin, containing at least one specific amphiphilic cationic polymer and at least one additional film-forming cationic and/or stabilizing polymer
DE102008038112A1 (en) 2008-08-18 2010-02-25 Henkel Ag & Co. Kgaa Agent for keratin-containing fibers containing at least one specific amphiphilic, cationic polymer and at least one polyol
US20110135591A1 (en) * 2008-08-18 2011-06-09 Burkhard Mueller Agent for fibers containing keratin, containing at least one specific amphiphilic cationic polymer and at least one additional film-forming cationic and/or stabilizing polymer
US20110135589A1 (en) * 2008-08-18 2011-06-09 Thorsten Knappe Product for keratin-containing fibers comprising at least one specific amphiphilic cationic polymer, and at least one specific amphiphilic anionic polymer
US20110132389A1 (en) * 2008-08-18 2011-06-09 Kaftan Pamela Agent for fibers containing keratin, comprising at least one specific amphiphilic cationic polymer, at least one cationic styling polymer that is different therefrom and at least one film-forming non-ionic and/or stabilizing non-ionic polymer
US20110142780A1 (en) * 2008-08-18 2011-06-16 Dirk Hentrich Agent for keratin-containing fibers, comprising at least one particular amphiphilic cationic polymer and at least one polymer with silicon-containing sidechains and anionic groups
US20110158928A1 (en) * 2008-08-18 2011-06-30 Burkhard Mueller Agent for fibres containing keratin, containing at least one specific amphiphilic cationic polymer and at least one specific, additional film-forming non-ionic and/or stabilizing non-ionic polymer
US20110165109A1 (en) * 2008-08-18 2011-07-07 Burkhard Mueller Agent for fibers containing keratin, comprising at least one specific amphiphilic cationic polymer and at least one additional film-forming and/or stabilizing polymer selected from chitosan and derivates thereof
DE102008038110A1 (en) 2008-08-18 2010-02-25 Henkel Ag & Co. Kgaa Keratin-containing fiber compositions comprising at least one specific amphiphilic cationic polymer and at least one additional special film-forming nonionic and / or setting nonionic polymer
DE102008038104A1 (en) 2008-08-18 2010-02-25 Henkel Ag & Co. Kgaa Agent for keratin-containing fibers containing at least one specific amphiphilic cationic polymer and at least one polymer with silicone-containing side chains and anionic groups
DE102008038107A1 (en) 2008-08-18 2010-02-25 Henkel Ag & Co. Kgaa Agent for keratin-containing fibers containing at least one particular amphiphilic cationic polymer and at least one additional film-forming and / or setting polymer selected from chitosan and its derivatives
DE102008038106A1 (en) 2008-08-18 2010-02-25 Henkel Ag & Co. Kgaa Keratin-containing fiber composition comprising at least one specific amphiphilic cationic polymer and at least one specific additional film-forming anionic and / or setting anionic polymer
DE102008059479A1 (en) 2008-11-28 2010-06-10 Henkel Ag & Co. Kgaa Agent, useful e.g. to treat human hair, comprises an amphiphilic, cationic polymer having pyrrolidin-2-one-, azepan-2-one- or nitrogen containing- structural unit, and a film-forming cationic and/or stabilizing cationic polymer
DE102008059480A1 (en) 2008-11-28 2010-06-02 Henkel Ag & Co. Kgaa Agent, useful e.g. to treat keratin fibers, comprises amphiphilic, cationic polymer having e.g. pyrrolidin-2-one structural unit, film-forming cationic/stabilizing cationic polymer, and film-forming non-ionic/stabilizing non-ionic polymer
DE102009031432A1 (en) 2009-07-01 2011-01-05 Henkel Ag & Co. Kgaa Compact hair spray
WO2011015512A2 (en) 2009-08-04 2011-02-10 Henkel Ag & Co. Kgaa Hair treatment products comprising specific polyethers and hair-fixing polymers
DE102009028209A1 (en) 2009-08-04 2011-02-10 Henkel Ag & Co. Kgaa Hair treatment compositions with polyether-modified organic compounds and hair-setting polymers
US8795642B2 (en) 2009-08-04 2014-08-05 Henkel Ag & Co. Kgaa Hair treatment agents comprising polyether-modified organic compounds and hair styling polymers
DE102009028206A1 (en) 2009-08-04 2011-02-10 Henkel Ag & Co. Kgaa Hair treatment products with special polyethers and hair-setting polymers
DE102009028207A1 (en) 2009-08-04 2011-02-17 Henkel Ag & Co. Kgaa Hair treatment agent with polyether-modified solid particles and hair-setting polymers
WO2013165648A1 (en) * 2012-05-02 2013-11-07 3M Innovative Properties Company Curable composition, articles comprising the curable composition, and method of making the same
US9056438B2 (en) 2012-05-02 2015-06-16 3M Innovative Properties Company Curable composition, articles comprising the curable composition, and method of making the same
CN105859544A (en) * 2016-04-21 2016-08-17 江南大学 High-purity oleic acid and preparation method thereof
DE102017100121A1 (en) 2017-01-04 2018-07-05 Franz Ferk Hair treatment agent for topical application
CN114349626A (en) * 2022-03-21 2022-04-15 佛山市滔盛弘新材料科技有限公司 Novel preparation method of C21 dibasic acid
DE202023103065U1 (en) 2023-06-04 2023-12-06 Lailuma Fanara Plant-based hair treatment products for topical application

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