GB424134A - Production of volatile compounds by fermentation - Google Patents

Production of volatile compounds by fermentation

Info

Publication number
GB424134A
GB424134A GB2277333A GB2277333A GB424134A GB 424134 A GB424134 A GB 424134A GB 2277333 A GB2277333 A GB 2277333A GB 2277333 A GB2277333 A GB 2277333A GB 424134 A GB424134 A GB 424134A
Authority
GB
United Kingdom
Prior art keywords
added
fermentation
produced
sugar
gas
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
GB2277333A
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.)
Henry Dreyfuss Associates LLC
Original Assignee
Henry Dreyfuss Associates LLC
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 Henry Dreyfuss Associates LLC filed Critical Henry Dreyfuss Associates LLC
Priority to GB2277333A priority Critical patent/GB424134A/en
Publication of GB424134A publication Critical patent/GB424134A/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
    • C12P1/00Preparation of compounds or compositions, not provided for in groups C12P3/00 - C12P39/00, by using microorganisms or enzymes
    • 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
    • C12P7/24Preparation of oxygen-containing organic compounds containing a carbonyl group
    • C12P7/26Ketones
    • C12P7/28Acetone-containing products

Abstract

Organic compounds produced by fermentation such as ethyl alcohol, or butyl alcohol and acetone, are removed by vaporization during the fermentation with the aid of a body forming an azeotropic mixture therewith, and, if desired, a gas may be passed through the liquor, but when the fermentation is anaerobic this gas should be free from oxygen. Suitable added liquids are hexane in the case of ethyl alcohol, and cyclohexane in the case of butyl alcohol and acetone. The liquid may be added continuously or intermittently and may be added in the form of vapour carried by the gas stream. Suitable additions of starting materials, ferments, or bacteria may be made to maintain the composition of the liquor constant. When using a top yeast, the enzyme effecting the change may be added, whereas with a bottom yeast it is preferred to add a co-enzyme. When producing alcohols, soluble phosphates may be added, preferably together with a body such as sodium arsenate, which prolongs the increased activity due to the addition of phosphate. When more than one product of fermentation is being produced, it is not necessary that the products should be removed in the same proportion in which they are produced. In an example, a solution of sugar, which may be produced from cellulose, is sterilized in a closed vessel, and a suitable yeast culture and suitable nutrients are added. The temperature is maintained at about 25 DEG C., hexane is introduced, and the pressure is reduced sufficiently to cause gentle boiling. During the process a sugar solution is added so as to maintain the concentration of the sugar constant, and other additions may be made.ALSO:Organic compounds produced by fermentation such as ethyl alcohol, or butyl alcohol and acetone, are removed by vaporization during the fermentation with the aid of a body forming an azeotropic mixture therewith, and, if desired, a gas may be passed through the liquor, but when the fermentation is anaerobic this gas should be free from oxygen. Suitable added liquids are hexane in the case of ethyl alcohol, and cyclohexane in the case of butyl alcohol and acetone. The liquid may be added continuously or intermittently and may be added in the form of vapour carried by the gas stream. Suitable additions of starting materials, ferments, or bacteria may be made to maintain the composition of the liquor constant. When using a top yeast, the enzyme effecting the change may be added, whereas with a bottom yeast it is preferred to add a co-enzyme. When producing alcohols soluble phosphates may be added, preferably together with a body such as sodium arsenate, which prolongs the increased activity due to the addition of phosphate. When more than one product of fermentation is being produced it is not necessary that the products should be removed in the same proportion in which they are produced. In an example, a solution of sugar, which may be produced from cellulose, is sterilized in a closed vessel, and a suitable yeast culture and suitable nutrients are added. The temperature is maintained at about 25 DEG C., hexane is introduced and the pressure is reduced sufficiently to cause gentle boiling. During the process a sugar solution is added so as to maintain the concentration of the sugar constant, and other additions may be made.ALSO:Organic compounds produced by fermentation, such as ethyl alcohol, or butyl alcohol and acetone, are removed by vaporization during the fermentation with the aid of a body forming an azeotropic mixture therewith, and, if desired, a gas may be passed through the liquor, but when the fermentation is anaerobic this gas should be free from oxygen. Suitable added liquids are hexane in the case of ethyl alcohol, and cyclohexane in the case of butyl alcohol and acetone. The liquid may be added continuously or intermittently, and may be added in the form of vapour carried by the gas stream. Suitable additions of starting materials, ferments, or bacteria may be made to maintain the composition of the liquor constant. When using a top yeast, the enzyme effecting the change may be added, whereas with a bottom yeast it is preferred to add a co-enzyme. When producing alcohols soluble phosphates may be added, preferably together with a body such as sodium arsenate, which prolongs the increased activity due to the addition of phosphate. When more than one product of fermentation is being produced it is not necessary that the products should be removed in the same proportion in which they are produced. In an example, a solution of sugar, which may be produced from cellulose, is sterilized in a closed vessel, and a suitable yeast culture and suitable nutrients are added. The temperature is maintained at about 25 DEG C., hexane is introduced and the pressure is reduced sufficiently to cause gentle boiling. During the process a sugar solution is added so as to maintain the concentration of the sugar constant, and other additions may be made.
GB2277333A 1933-08-15 1933-08-15 Production of volatile compounds by fermentation Expired GB424134A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
GB2277333A GB424134A (en) 1933-08-15 1933-08-15 Production of volatile compounds by fermentation

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB2277333A GB424134A (en) 1933-08-15 1933-08-15 Production of volatile compounds by fermentation

Publications (1)

Publication Number Publication Date
GB424134A true GB424134A (en) 1935-02-15

Family

ID=10184835

Family Applications (1)

Application Number Title Priority Date Filing Date
GB2277333A Expired GB424134A (en) 1933-08-15 1933-08-15 Production of volatile compounds by fermentation

Country Status (1)

Country Link
GB (1) GB424134A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4361586A (en) * 1980-11-12 1982-11-30 Meinke Wilmon W Vacuum enzymatic digestion of protein material

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4361586A (en) * 1980-11-12 1982-11-30 Meinke Wilmon W Vacuum enzymatic digestion of protein material

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