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GB822154A - Fermentation process for the production of d-arabitol - Google Patents

Fermentation process for the production of d-arabitol

Info

Publication number
GB822154A
GB822154A GB486457A GB486457A GB822154A GB 822154 A GB822154 A GB 822154A GB 486457 A GB486457 A GB 486457A GB 486457 A GB486457 A GB 486457A GB 822154 A GB822154 A GB 822154A
Authority
GB
United Kingdom
Prior art keywords
arabitol
source
nutrient medium
preferred
medium
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
GB486457A
Inventor
Owen Lavin
John William Holloway
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.)
Commercial Solvents Great Britain Ltd
Original Assignee
Commercial Solvents Great Britain 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 Commercial Solvents Great Britain Ltd filed Critical Commercial Solvents Great Britain Ltd
Priority to GB486457A priority Critical patent/GB822154A/en
Publication of GB822154A publication Critical patent/GB822154A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12PFERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
    • C12P7/00Preparation of oxygen-containing organic compounds
    • C12P7/02Preparation of oxygen-containing organic compounds containing a hydroxy group
    • C12P7/04Preparation of oxygen-containing organic compounds containing a hydroxy group acyclic
    • C12P7/18Preparation of oxygen-containing organic compounds containing a hydroxy group acyclic polyhydric

Landscapes

  • Organic Chemistry (AREA)
  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Zoology (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Wood Science & Technology (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Microbiology (AREA)
  • General Chemical & Material Sciences (AREA)
  • Biotechnology (AREA)
  • Health & Medical Sciences (AREA)
  • Biochemistry (AREA)
  • Bioinformatics & Cheminformatics (AREA)
  • General Engineering & Computer Science (AREA)
  • General Health & Medical Sciences (AREA)
  • Genetics & Genomics (AREA)
  • Micro-Organisms Or Cultivation Processes Thereof (AREA)
  • Preparation Of Compounds By Using Micro-Organisms (AREA)

Abstract

Glycerol is prepared by fermenting a suitable nutrient medium under submerged and aerated conditions with a d-arabitol-producing strain of Saccharomyces rouxii or Saccaromyces mellis, the nutrient medium containing high-test cane molasses as the major source of assimilable carbon and also a further source of nitrogen such as urea, e.g. 0.05-0.1% w/v. It is preferred to add a further small proportion of an organic nitrogen source such as corn-steep liquor or yeast extract, e.g. 0.3-1.5% w/v. Invertase may also be added, e.g. about 0.02 to 0.3% w/v. Preferred total sugar concentration in the medium is about 15-25% w/v. Fermentation temperatures of about 30-37 DEG C. are suitable. The glycerine may be recovered by steam-distillation from the d-arabitol-containing ferment.ALSO:D-arabitol is prepared by fermenting under submerged and aerated conditions, a suitable nutrient medium with a d-arabitol-producing strain of Saccharomyces rouxii or Saccharomyces mellis wherein the nutrient medium contains high test cane molasses as the major source of assimilable carbon and also a further source of simple nitrogen such as urea, e.g. 0.05-0.1% w/v. It is preferred to add a further small proportion of an organic nitrogen source such as corn steep liquor or yeast extract, e.g. 0.3-1.5% w/v. Invertase may also be added, e.g. about 0.02 to 0.03% v/v. Preferred total sugar concentration in the medium is about 15-25% w/v. Fermentation temperatures of about 30-37 DEG C. are suitable. The d-arabitol may be recovered by extraction with a lower aliphatic alcohol after concentration.
GB486457A 1957-02-13 1957-02-13 Fermentation process for the production of d-arabitol Expired GB822154A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
GB486457A GB822154A (en) 1957-02-13 1957-02-13 Fermentation process for the production of d-arabitol

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB486457A GB822154A (en) 1957-02-13 1957-02-13 Fermentation process for the production of d-arabitol

Publications (1)

Publication Number Publication Date
GB822154A true GB822154A (en) 1959-10-21

Family

ID=9785253

Family Applications (1)

Application Number Title Priority Date Filing Date
GB486457A Expired GB822154A (en) 1957-02-13 1957-02-13 Fermentation process for the production of d-arabitol

Country Status (1)

Country Link
GB (1) GB822154A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4271268A (en) 1977-09-12 1981-06-02 Hoffmann-La Roche Inc. Process for producing D-arabitol
WO2010022045A1 (en) * 2008-08-20 2010-02-25 Novozymes A/S Processes for producing fermentation products

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4271268A (en) 1977-09-12 1981-06-02 Hoffmann-La Roche Inc. Process for producing D-arabitol
WO2010022045A1 (en) * 2008-08-20 2010-02-25 Novozymes A/S Processes for producing fermentation products

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