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EP0040346A1 - Procédé de raffinage de produit brut de condensation à partir d'aminoalcoylalcanolamines et acides gras ainsi que, le cas échéant, pour la récupération subséquente d'amphotensides à stabilité plus élevée - Google Patents

Procédé de raffinage de produit brut de condensation à partir d'aminoalcoylalcanolamines et acides gras ainsi que, le cas échéant, pour la récupération subséquente d'amphotensides à stabilité plus élevée Download PDF

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Publication number
EP0040346A1
EP0040346A1 EP81103328A EP81103328A EP0040346A1 EP 0040346 A1 EP0040346 A1 EP 0040346A1 EP 81103328 A EP81103328 A EP 81103328A EP 81103328 A EP81103328 A EP 81103328A EP 0040346 A1 EP0040346 A1 EP 0040346A1
Authority
EP
European Patent Office
Prior art keywords
condensation product
fatty acids
mol
product
alkaline
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
EP81103328A
Other languages
German (de)
English (en)
Other versions
EP0040346B1 (fr
Inventor
Uwe Dr. Ploog
Günter Uphues
Manfred Petzold
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Henkel AG and Co KGaA
Original Assignee
Henkel AG and Co KGaA
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Henkel AG and Co KGaA filed Critical Henkel AG and Co KGaA
Priority to AT81103328T priority Critical patent/ATE5815T1/de
Publication of EP0040346A1 publication Critical patent/EP0040346A1/fr
Application granted granted Critical
Publication of EP0040346B1 publication Critical patent/EP0040346B1/fr
Expired legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11DDETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
    • C11D1/00Detergent compositions based essentially on surface-active compounds; Use of these compounds as a detergent
    • C11D1/88Ampholytes; Electroneutral compounds

Definitions

  • amphoteric surfactants An important process for the production of amphoteric surfactants is based on condensation products of N-monosubstituted alkylenediamines, which are alkylated in a further reaction with alkylating agents, for example sodium chloroacetate. Products based on N-aminoethylethanolamine and fatty acids play a major role as skin-friendly surfactants.
  • the quality of the amphoteric surfactants obtained and in particular their storage stability is crucially determined by the purity of the imidazoline derivative obtained in the first condensation step.
  • the reaction between fatty acids and Aminoalkylalkanolaminen extends not only towards the formation of the desired Imidazolinderiva- t s e, multiple side reactions complicate the reaction. The importance of this aspect has been exposed again only recently, see EC Lomax "N ew and improved balanced amphoterics" Manufacturing Chemist and Aerosol News, Volume 50 no. 8, August 1979, pages 39 and 41.
  • Described here is, for example, that the undesired side reactions in the stage of imidazoline formation can be suppressed by an excess of aminoethylethanolamine, but this excess must be removed by distillation at the end of the reaction. Excess aminoethylethanolamine, in turn, can create new difficulties by cycling to piperazine.
  • the purity of the imidazoline obtained in the first reaction stage has a decisive influence on the storage stability of the amphoteric surfactants or their aqueous solutions obtained by subsequent alkylation. Even a small amount of contamination leads to the separation of a solid phase after a shorter or longer storage period, be it in the form of cloudiness or precipitation. Such products are unusable for practical use or at least of limited value.
  • the invention is based on the object of creating improvements in the production of the class of amphoteric surfactants described here, which are characterized in particular by increased storage stability of the amphoteric surfactants.
  • the invention aims to eliminate the troublesome by-products present here by switching on a simple cleaning step on the condensate of aminoalkylalkanolamine and fatty acid obtained in the first place.
  • the invention is intended to make the previously expensive detours for obtaining the purest possible condensation product of this first process stage superfluous.
  • the teaching of the invention is based on the surprising finding that the crude condensation product of fatty acids and aminoalkylalkanolamines can be converted by simple alkaline hydrolysis to a refined product which, in the subsequent alkylation and optionally quaternization, provides improved amphoteric surfactants with, in particular, increased storage stability.
  • the invention accordingly relates to a process for refining the crude condensation product from aminoalkylalkanolamines of the general formula and fatty acids having 6 to 22 carbon atoms and, if desired, for subsequent alkylation and, if appropriate, quaternization of the purified condensation product to amphoteric surfactants with increased storage stability, this process being characterized in that the crude condensation product of fatty acids and aminoalkylalkanolamines is subjected to alkaline hydrolysis.
  • the amount of alkali used in this alkaline hydrolysis is preferably based on the amount of the diamide of the general formula present in the crude condensate Voted.
  • the amount of alkali is dimensioned in this process stage so that it is preferred is present in the crude condensation product in at least approximately an equimolar amount to the diamide.
  • the invention is based on the finding that the content of disruptive by-products in the finished surfactant can be drastically reduced if the fatty acid / amine condensation product is subjected to an alkaline pretreatment in an aqueous medium before a further reaction with alkylating agents.
  • diamide formed in particular in the course of the reaction by aqueous alkali on the tert.
  • Amide group quantitatively split into the monoamide of the primary amino group and fatty acid.
  • the fatty acid forms soap which can remain in the reaction mixture.
  • the alkaline pretreatment according to the invention gives products which remain clear even after dilution for longer than 6 months. Costly cleaning steps such as recovery of the excess amine or distillation of the imidazoline are no longer necessary.
  • the alkaline hydrolytic treatment according to the invention is preferably carried out at temperatures of approximately 70 to 100 ° C., in particular in the temperature range of 80 to 90 ° C.
  • Alkali hydroxides, especially sodium hydroxide are particularly suitable as alkalis.
  • the amount of alkali is preferably in the range of about 1 to 3 times the eguimolar alkali requirement, based on the diamide present in the crude condensation product. In particular, alkali amounts in the range of 1 to 2 equivalents, based on diamide, are used.
  • the crude condensation product is expediently suspended in an amount of water which corresponds to 0.5 to 10 times, in particular 1 to 5 times, the crude condensation product.
  • the aqueous alkaline hydrolysis is carried out until the diamide present as a by-product is virtually completely eliminated.
  • the diamide content of the crude product and its decrease in the treatment according to the invention can be e.g. can be determined by working with ion exchangers.
  • aminoalkylalkanolamines of the general formula those compounds are used in which m has the value from 2 to 6 and n has the value from 2 or 3.
  • the meaning of m is preferably 2, 3 or 6, the preferred meaning for n is 2.
  • the most important starting amine in practice of the type concerned here is aminoethylethanolamine.
  • the fatty acids related to the condensation have carbon numbers in the range from 6 to 22, with particular importance in the range from 8 to 18 carbon atoms Has.
  • the carboxylic acids can be present as pure components or as mixtures. They can be of natural and / or synthetic origin.
  • the condensation product pretreated in the sense of the invention by the alkaline hydrolysis is then converted in a manner known per se to the finished amphoteric surfactant.
  • the pretreatment according to the invention proves to be valuable not only for the production of the so-called imidazolinium surfactants, but rather it can be used in many different ways.
  • amphoteric surfactants can have alkylated and optionally quaternized nitrogen in the second reaction stage.
  • the invention comprises the production of such amphoteric surfactants using a condensation precursor which has been treated according to the alkaline hydrolytic process of the invention described.
  • the percentages relate to% by weight.
  • the diamide content is determined as follows: The condensation product is sent as an alcoholic solution through a strongly acidic ion exchanger. The eluate is evaporated and the remaining residue is related to the weight. By determining the S.Z. and the total nitrogen, the amount of diamide can be calculated.
  • Imidazoline content 3.0%
  • the product is clear as in 2.1.1, but also clouded after 6 days because not all diamide has been saponified.
  • the finished product is clear and thin, but shows deposits after 2 days.
  • the end product is clear, but becomes cloudy after 3 days.
  • the product is still clear after more than 6 months.

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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)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Detergent Compositions (AREA)
  • Photovoltaic Devices (AREA)
  • Fats And Perfumes (AREA)
EP81103328A 1980-05-13 1981-05-02 Procédé de raffinage de produit brut de condensation à partir d'aminoalcoylalcanolamines et acides gras ainsi que, le cas échéant, pour la récupération subséquente d'amphotensides à stabilité plus élevée Expired EP0040346B1 (fr)

Priority Applications (1)

Application Number Priority Date Filing Date Title
AT81103328T ATE5815T1 (de) 1980-05-13 1981-05-02 Verfahren zur raffination des rohen kondensationsproduktes aus aminoalkylalkanolaminen und fettsaeuren sowie gewuenschtenfalls zur anschliessenden gewinnung von amphotensiden mit erhoehter lagerstabilitaet.

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE19803018201 DE3018201A1 (de) 1980-05-13 1980-05-13 Verfahren zur raffination des rohen kondensationsproduktes aus aminoalkylalkanolaminen und fettsaeuren sowie gewuenschtenfalls zur anschliessenden gewinnung von amphotensiden mit erhoehter lagerstabilitaet
DE3018201 1980-05-13

Publications (2)

Publication Number Publication Date
EP0040346A1 true EP0040346A1 (fr) 1981-11-25
EP0040346B1 EP0040346B1 (fr) 1984-01-11

Family

ID=6102253

Family Applications (1)

Application Number Title Priority Date Filing Date
EP81103328A Expired EP0040346B1 (fr) 1980-05-13 1981-05-02 Procédé de raffinage de produit brut de condensation à partir d'aminoalcoylalcanolamines et acides gras ainsi que, le cas échéant, pour la récupération subséquente d'amphotensides à stabilité plus élevée

Country Status (9)

Country Link
EP (1) EP0040346B1 (fr)
JP (1) JPS5716846A (fr)
AT (1) ATE5815T1 (fr)
AU (1) AU541532B2 (fr)
BR (1) BR8102948A (fr)
CA (1) CA1214778A (fr)
DE (2) DE3018201A1 (fr)
ES (1) ES502137A0 (fr)
MX (1) MX156685A (fr)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4833253A (en) * 1986-12-08 1989-05-23 Henkel Kommanditgesellschaft Auf Aktien Process for the production of low-viscosity amphoteric surfactants
US5342961A (en) * 1990-12-06 1994-08-30 Henkel Kommanditgesellschaft Auf Aktien Process for the production of low-viscosity imidazolinium surfactants by quaternization of 1-hydroxyethyl-2-alkyl imidazolines
EP0647469A3 (fr) * 1993-10-12 1996-04-03 Rhone Poulenc Spec Chim Amphoacétates tensio-actifs de plus grande pureté, dérivés de l'imidazoline, et leurs procédés de préparation.
US5569767A (en) * 1992-11-30 1996-10-29 Henkel Kommanditgesellschaft Auf Aktien Process for the production of low-viscosity storable amphoteric surfactants from imidazolines
EP0872576A1 (fr) * 1997-04-14 1998-10-21 Clariant GmbH Amphoglycinates comme inhibiteurs de la corrosion de métaux ferreux et non-ferreux

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE3444864A1 (de) * 1984-12-08 1986-06-12 Henkel KGaA, 4000 Düsseldorf Verfahren zur fettung von leder und pelzen

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2752116A1 (de) * 1976-12-01 1978-06-29 Lion Fat Oil Co Ltd Disubstituiertes aliphatisches carbonsaeureamidamin, verfahren zu seiner herstellung und es enthaltende mittel
EP0001006A1 (fr) * 1977-08-18 1979-03-07 Albright & Wilson Limited Dérivés carboalkylés d'éthylène-diamines acylées, procédé pour leur préparation et compositions tensio-actives

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5938221B2 (ja) * 1976-01-20 1984-09-14 ライオン株式会社 第四級アンモニウム塩の製造方法
JPS5951532B2 (ja) * 1976-09-03 1984-12-14 川研フアインケミカル株式会社 新規なアミンアミド化合物,その製造方法および前記アミンアミド化合物を含有する界面活性剤

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2752116A1 (de) * 1976-12-01 1978-06-29 Lion Fat Oil Co Ltd Disubstituiertes aliphatisches carbonsaeureamidamin, verfahren zu seiner herstellung und es enthaltende mittel
EP0001006A1 (fr) * 1977-08-18 1979-03-07 Albright & Wilson Limited Dérivés carboalkylés d'éthylène-diamines acylées, procédé pour leur préparation et compositions tensio-actives

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4833253A (en) * 1986-12-08 1989-05-23 Henkel Kommanditgesellschaft Auf Aktien Process for the production of low-viscosity amphoteric surfactants
EP0275421A3 (en) * 1986-12-08 1990-11-22 Henkel Kommanditgesellschaft Auf Aktien Process for the preparation of highly viscous amphotensides
US5342961A (en) * 1990-12-06 1994-08-30 Henkel Kommanditgesellschaft Auf Aktien Process for the production of low-viscosity imidazolinium surfactants by quaternization of 1-hydroxyethyl-2-alkyl imidazolines
US5569767A (en) * 1992-11-30 1996-10-29 Henkel Kommanditgesellschaft Auf Aktien Process for the production of low-viscosity storable amphoteric surfactants from imidazolines
EP0647469A3 (fr) * 1993-10-12 1996-04-03 Rhone Poulenc Spec Chim Amphoacétates tensio-actifs de plus grande pureté, dérivés de l'imidazoline, et leurs procédés de préparation.
US5744063A (en) * 1993-10-12 1998-04-28 Rhone-Poulenc Inc. Higher purity imidazoline based amphoacetate surfactants and processes for the preparation thereof
US5952291A (en) * 1993-10-12 1999-09-14 Rhodia Inc. Process for the preparation of high purity imidazoline based amphoacetate surfactants
US6057282A (en) * 1993-10-12 2000-05-02 Rhodia Inc. High purity imidazoline-based amphoacetate surfactants
EP0872576A1 (fr) * 1997-04-14 1998-10-21 Clariant GmbH Amphoglycinates comme inhibiteurs de la corrosion de métaux ferreux et non-ferreux

Also Published As

Publication number Publication date
AU7051181A (en) 1981-11-19
BR8102948A (pt) 1982-02-02
ATE5815T1 (de) 1984-01-15
ES8203830A1 (es) 1982-04-01
DE3018201A1 (de) 1981-11-19
DE3161875D1 (en) 1984-02-16
AU541532B2 (en) 1985-01-10
JPS5716846A (en) 1982-01-28
EP0040346B1 (fr) 1984-01-11
CA1214778A (fr) 1986-12-02
ES502137A0 (es) 1982-04-01
JPH0249299B2 (fr) 1990-10-29
MX156685A (es) 1988-09-26

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