GB826801A - Recovery of sucrose esters - Google Patents

Recovery of sucrose esters

Info

Publication number
GB826801A
GB826801A GB2718857A GB2718857A GB826801A GB 826801 A GB826801 A GB 826801A GB 2718857 A GB2718857 A GB 2718857A GB 2718857 A GB2718857 A GB 2718857A GB 826801 A GB826801 A GB 826801A
Authority
GB
United Kingdom
Prior art keywords
solvent
sucrose
ester
esters
aliphatic
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
GB2718857A
Inventor
Bernard Hammond Markh Thompson
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.)
Distillers Co Yeast Ltd
Distillers Co Ltd
Original Assignee
Distillers Co Yeast Ltd
Distillers Co Ltd
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 Distillers Co Yeast Ltd, Distillers Co Ltd filed Critical Distillers Co Yeast Ltd
Priority to GB2718857A priority Critical patent/GB826801A/en
Publication of GB826801A publication Critical patent/GB826801A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07HSUGARS; DERIVATIVES THEREOF; NUCLEOSIDES; NUCLEOTIDES; NUCLEIC ACIDS
    • C07H13/00Compounds containing saccharide radicals esterified by carbonic acid or derivatives thereof, or by organic acids, e.g. phosphonic acids
    • C07H13/02Compounds containing saccharide radicals esterified by carbonic acid or derivatives thereof, or by organic acids, e.g. phosphonic acids by carboxylic acids
    • C07H13/04Compounds containing saccharide radicals esterified by carbonic acid or derivatives thereof, or by organic acids, e.g. phosphonic acids by carboxylic acids having the esterifying carboxyl radicals attached to acyclic carbon atoms
    • C07H13/06Fatty acids

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Biochemistry (AREA)
  • Biotechnology (AREA)
  • General Health & Medical Sciences (AREA)
  • Genetics & Genomics (AREA)
  • Molecular Biology (AREA)
  • Saccharide Compounds (AREA)

Abstract

Esters of sucrose with aliphatic monocarboxylic acids are recovered from crude reaction mixtures containing such esters by removing at least 90% by weight of the reaction solvent, then contacting the remaining crude reaction mixture with water and a partially watermiscible ketone solvent or ester solvent to form an aqueous phase and a solvent phase, whereby the sucrose ester is extracted into the solvent phase, separating the solvent phase and recovering the sucrose ester therefrom. The process is preferably used to recover mono- and di-esters of sucrose and aliphatic acids containing at least 8 carbon atoms. The initial esterification suitably employs a solvent of relatively high boiling point such as dimethylformamide and the removal of at least 90% by weight of the solvent is preferably effected by distillation under reduced pressure. Suitable ketones are aliphatic and cycloaliphatic ketones containing up to 8 carbon atoms per molecule, methyl isobutyl ketone being preferred. Suitable esters are those containing at least 6 carbon atoms and derived from an aliphatic carboxylic acid and an aliphatic monohydric alcohol. The amount of water and ketone or ester solvent is suitably about twice the volume of the reaction mixture. The extraction may be effected at 40 DEG to 80 DEG C. and preferably while maintaining a neutral or slightly acid r H, e.g. 4-7, if necessary by adding acidic substances. The extraction may be carried out batchwise or continuously using a counter-current procedure. Preferably the solvent phase containing the sucrose ester is further contacted with water to form two phases, to remove the last traces of reaction solvent and sucrose into the aqueous phase. In a countercurrent system the outgoing solvent phase encounters a feed of fresh water shortly before leaving the system. The ester may be recovered from the solvent phase by distilling off the ketone or ester in the presence of water, leaving a solution or slurry of product which may be spray dried or drum dried. Alternatively, the water present in the solvent phase may be distilled as an azeotrope with the solvent using a decanting-type still head which continuously returns the solvent phase to the still. The ester may then be recovered by distillation of the solvent or by concentration and crystallization of the sucrose ester. Examples describe the preparation of sucrose esters by reacting sucrose with an alkyl ester of an aliphatic acid in dimethylformamide at elevated temperature in the presence of potassium carbonate as catalyst, and the recovery of the sucrose esters as described above.
GB2718857A 1957-08-29 1957-08-29 Recovery of sucrose esters Expired GB826801A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
GB2718857A GB826801A (en) 1957-08-29 1957-08-29 Recovery of sucrose esters

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB2718857A GB826801A (en) 1957-08-29 1957-08-29 Recovery of sucrose esters

Publications (1)

Publication Number Publication Date
GB826801A true GB826801A (en) 1960-01-20

Family

ID=10255630

Family Applications (1)

Application Number Title Priority Date Filing Date
GB2718857A Expired GB826801A (en) 1957-08-29 1957-08-29 Recovery of sucrose esters

Country Status (1)

Country Link
GB (1) GB826801A (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1205510B (en) * 1961-09-12 1965-11-25 Ledoga Spa Process for the quantitative separation of pure cane sugar mono- or diesters of saturated or unsaturated fatty acids with 6 to 30 carbon atoms
US3347848A (en) * 1964-07-08 1967-10-17 Ismail Roshdy Process for the production of sucrose esters of fatty acids
DE2004899A1 (en) * 1969-02-05 1970-09-03
EP0020122A1 (en) * 1979-05-24 1980-12-10 TATE & LYLE PATENT HOLDINGS LIMITED Process for the preparation of sucrose monoesters
GB2163425A (en) * 1984-08-10 1986-02-26 Nebraska State Separation and purification of sugar esters
US4710567A (en) * 1984-08-10 1987-12-01 Nebraska Department Of Economic Development, State Of Nebraska Separation and purification of sugar esters synthesized from both aqueous and nonaqueous systems
EP0659760A2 (en) * 1993-12-24 1995-06-28 Mitsubishi Chemical Corporation Process for producing sucrose fatty acid ester

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1205510B (en) * 1961-09-12 1965-11-25 Ledoga Spa Process for the quantitative separation of pure cane sugar mono- or diesters of saturated or unsaturated fatty acids with 6 to 30 carbon atoms
US3347848A (en) * 1964-07-08 1967-10-17 Ismail Roshdy Process for the production of sucrose esters of fatty acids
DE2004899A1 (en) * 1969-02-05 1970-09-03
EP0020122A1 (en) * 1979-05-24 1980-12-10 TATE & LYLE PATENT HOLDINGS LIMITED Process for the preparation of sucrose monoesters
GB2163425A (en) * 1984-08-10 1986-02-26 Nebraska State Separation and purification of sugar esters
US4710567A (en) * 1984-08-10 1987-12-01 Nebraska Department Of Economic Development, State Of Nebraska Separation and purification of sugar esters synthesized from both aqueous and nonaqueous systems
EP0659760A2 (en) * 1993-12-24 1995-06-28 Mitsubishi Chemical Corporation Process for producing sucrose fatty acid ester
EP0659760A3 (en) * 1993-12-24 1995-10-25 Mitsubishi Chem Corp Process for producing sucrose fatty acid ester.
US5565557A (en) * 1993-12-24 1996-10-15 Mitsubishi Chemical Corporation Process for producing sucrose fatty acid ester

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