GB950667A - Process for the preparation of monoglycerides - Google Patents

Process for the preparation of monoglycerides

Info

Publication number
GB950667A
GB950667A GB33446/61A GB3344661A GB950667A GB 950667 A GB950667 A GB 950667A GB 33446/61 A GB33446/61 A GB 33446/61A GB 3344661 A GB3344661 A GB 3344661A GB 950667 A GB950667 A GB 950667A
Authority
GB
United Kingdom
Prior art keywords
glycerine
mol
fatty acids
reaction
alcohols
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.)
Expired
Application number
GB33446/61A
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
Publication of GB950667A publication Critical patent/GB950667A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11CFATTY ACIDS FROM FATS, OILS OR WAXES; CANDLES; FATS, OILS OR FATTY ACIDS BY CHEMICAL MODIFICATION OF FATS, OILS, OR FATTY ACIDS OBTAINED THEREFROM
    • C11C3/00Fats, oils, or fatty acids by chemical modification of fats, oils, or fatty acids obtained therefrom
    • C11C3/02Fats, oils, or fatty acids by chemical modification of fats, oils, or fatty acids obtained therefrom by esterification of fatty acids with glycerol
    • C11C3/025Fats, oils, or fatty acids by chemical modification of fats, oils, or fatty acids obtained therefrom by esterification of fatty acids with glycerol with a stoechiometric excess of glycerol
    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11CFATTY ACIDS FROM FATS, OILS OR WAXES; CANDLES; FATS, OILS OR FATTY ACIDS BY CHEMICAL MODIFICATION OF FATS, OILS, OR FATTY ACIDS OBTAINED THEREFROM
    • C11C3/00Fats, oils, or fatty acids by chemical modification of fats, oils, or fatty acids obtained therefrom
    • C11C3/04Fats, oils, or fatty acids by chemical modification of fats, oils, or fatty acids obtained therefrom by esterification of fats or fatty oils
    • C11C3/06Fats, oils, or fatty acids by chemical modification of fats, oils, or fatty acids obtained therefrom by esterification of fats or fatty oils with glycerol

Landscapes

  • Chemical & Material Sciences (AREA)
  • General 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)
  • Fats And Perfumes (AREA)

Abstract

Glycerides having a high monoglyceride content are prepared by a process which comprises the reaction, in a medium which contains at least 50 mols per cent glycerine, 35-10 mol per cent monoglyceride and not more than 15 mol per cent di- and tri-glycerides, at a temperature of at least 260 DEG C., of the components of an agent consisting of compounds from which the monoglyceride may be formed, wherein in said agent at least 2 mol and preferably 3-5 mol glyceride radicals are used per mol of added fatty acid radical, said agent being employed in an amount not more than 0.5 parts by weight and preferably not more than 0.4 parts by weight of the reaction medium, the agent being added during the reaction to maintain said proportion thereof, the expression "components from which the monoglyceride may be formed" being defined as "a mixture of glycerine and fatty acids or their esters with glycerine or other mono- or polyvalent alcohols provided that the other alcohols are more volatile than glycerine". The reaction products comprising glycerine and a glyceride having a high monoglyceride content are preferably separated into two layers by cooling, one layer comprising glycerine which is removed, the remaining glycerine being removed from the other layer by distillation. An extensive purification of the monoglyceride by water-washing is described. The fatty acids are preferably saturated or unsaturated C10-20 fatty acids of natural origin such as occur in the fats of vegetation and of land and aquatic animals, but the hydrogenation products of natural fatty acids and synthetic straight or branched-chain fatty acids may also be used. Suitable esters of these acids include esters with C1-4 alcohols such as methyl and ethyl alcohols and ethylene and propylene glycols. Conventional esterification or re-esterification catalysts such as metal oxides, hydroxides or alcoholates, or free metals, may optionally be added. Examples describe the reaction together in appropriate media of glycerine and (1) hydrogenated tallow fatty acid, (2) a C12-18 fraction of a coconut fatty acid, (3) lauric acid, (4) olive oil, and (5) methyl laurate.ALSO:Glycerides having a high monoglyceride content are prepared by reacting at a temperature of at least 260 DEG C. in a medium which contains at least 50 mols. per cent glycerine, 35-10 mol. per cent mono-glyceride and not more than 15 mol. per cent di- and tri-glycerides, a mixture of glycerine and fatty acids or their esters with glycerine or other mono- or polyvalent alcohols (provided that the other alcohols are more volatile than glycerine), containing at least 2 mol., preferably 3-5 mol., glyceride radicals per mol. of added fatty acid radical, the mixture, which is added during the reaction to maintain said proportions being present in an amount not more than 0.5 parts, preferably not more than 0.4 parts, by weight of the reaction medium. The reaction products comprising glycerine and a glyceride having a high monoglyceride content are preferably separated into two layers by cooling, one layer comprising glycerine which is removed; residual glycerine is removed from the other layer by distillation. An extensive purification of the monoglyceride by water-washing is described. The fatty acids are preferably saturated or unsaturated C10-20 fatty acids derived from vegetable, animal and marine fats, but the hydrogenated natural fatty acids and synthetic straight or branched-chain fatty acids may also be used. Suitable esters of these acids include esters with C1-4 alcohols such as methyl and ethyl alcohols and ethylene and propylene glycols. Conventional esterification or re-esterification catalysts such as metal oxides, hydroxides or alcoholates, or free metals, may optionally be added. Examples describe the reaction together in appropriate media of glycerine and (1) hydrogenated tallow fatty acid, (2) a C12-18 fraction of a coconut fatty acid, (3) lauric acid, (4) olive oil, and (5) methyl laurate.
GB33446/61A 1960-10-11 1961-09-19 Process for the preparation of monoglycerides Expired GB950667A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DEH40631A DE1206881B (en) 1960-10-11 1960-10-11 Process for the production of fatty acid glyceride mixtures with a high monoglyceride content

Publications (1)

Publication Number Publication Date
GB950667A true GB950667A (en) 1964-02-26

Family

ID=7154316

Family Applications (1)

Application Number Title Priority Date Filing Date
GB33446/61A Expired GB950667A (en) 1960-10-11 1961-09-19 Process for the preparation of monoglycerides

Country Status (7)

Country Link
US (1) US3160646A (en)
BE (1) BE609023A (en)
DE (1) DE1206881B (en)
DK (1) DK118714B (en)
FR (1) FR1316499A (en)
GB (1) GB950667A (en)
NL (1) NL270102A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
AU2002347198B2 (en) * 2001-12-13 2008-04-17 Jott Australia Pty Ltd Process for production of fatty acid esters

Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
LU66093A1 (en) * 1972-09-15 1974-03-25
MY129120A (en) * 1997-08-19 2007-03-30 Global Palm Products Sdn Bhd Process for the production of monoglyceride based on the glycerolysis of methyl ester
US20050048187A1 (en) * 2003-06-04 2005-03-03 Jim Doucet Shortening system
MXPA06001962A (en) * 2003-08-21 2006-05-17 Danisco Shortening system.
US20100148117A1 (en) * 2008-12-11 2010-06-17 Logan Roger L Method of making glycerol monoesters
WO2017085737A1 (en) * 2015-11-19 2017-05-26 Fine Research & Development Centre Pvt Ltd A natural based monoglyceride with improved odor and flavor
KR102043442B1 (en) * 2019-02-01 2019-11-11 주식회사 천강 Method for manufacturing low-valuable Glyceride for Biodiesel Feedstock

Family Cites Families (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2732387A (en) * 1956-01-24 Method of making monoglycerides
US2022494A (en) * 1935-02-14 1935-11-26 Armour & Co Process of preparing mono and di-glycerides
US2383581A (en) * 1943-05-06 1945-08-28 Colgate Palmolive Peet Co Process for preparing fatty materials
US2478354A (en) * 1946-04-26 1949-08-09 Colgate Paimolive Peet Company Preparation of partial esters
US2759954A (en) * 1949-02-02 1956-08-21 Chemical Foundation Inc Refining crude fatty acid monoglyceride
FR980205A (en) * 1949-02-07 1951-05-09 Paix & Cie Process for preparing wetting, foaming, detergents and m? Lsion nants
US2634279A (en) * 1949-07-16 1953-04-07 Eastman Kodak Co Preparation of monoglycerides
US2634278A (en) * 1949-07-16 1953-04-07 Eastman Kodak Co Process for substantially complete conversion of fatty material to partial ester
US2727913A (en) * 1952-10-11 1955-12-20 Eastman Kodak Co Method of obtaining concentrated monoglycerides
US2744124A (en) * 1952-11-28 1956-05-01 Colgate Palmolive Co Process for preparing fatty acid partial esters of polyhydric alcohols
US2789119A (en) * 1954-02-09 1957-04-16 Boake Roberts & Co Ltd Production of fatty acid monoglycerides

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
AU2002347198B2 (en) * 2001-12-13 2008-04-17 Jott Australia Pty Ltd Process for production of fatty acid esters

Also Published As

Publication number Publication date
FR1316499A (en) 1963-02-01
BE609023A (en) 1962-02-01
US3160646A (en) 1964-12-08
NL270102A (en)
DE1206881B (en) 1965-12-16
DK118714B (en) 1970-09-28

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