EP0051653A1 - Preparation of ethanol with immobilized microorganism - Google Patents

Preparation of ethanol with immobilized microorganism

Info

Publication number
EP0051653A1
EP0051653A1 EP81901325A EP81901325A EP0051653A1 EP 0051653 A1 EP0051653 A1 EP 0051653A1 EP 81901325 A EP81901325 A EP 81901325A EP 81901325 A EP81901325 A EP 81901325A EP 0051653 A1 EP0051653 A1 EP 0051653A1
Authority
EP
European Patent Office
Prior art keywords
lactose
microorganism
fermentation
fermenting
ethanol
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.)
Withdrawn
Application number
EP81901325A
Other languages
German (de)
French (fr)
Inventor
Niels Bayer
Sven Erik Godtfredsen
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.)
DuPont Nutrition Biosciences ApS
De Forenede Bryggerier AS
Original Assignee
Danske Spritfabrikker AS
Danisco AS
De Forenede Bryggerier AS
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 Danske Spritfabrikker AS, Danisco AS, De Forenede Bryggerier AS filed Critical Danske Spritfabrikker AS
Publication of EP0051653A1 publication Critical patent/EP0051653A1/en
Withdrawn legal-status Critical Current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
    • C12P7/06Ethanol, i.e. non-beverage
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12NMICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
    • C12N11/00Carrier-bound or immobilised enzymes; Carrier-bound or immobilised microbial cells; Preparation thereof
    • C12N11/02Enzymes or microbial cells immobilised on or in an organic carrier
    • C12N11/04Enzymes or microbial cells immobilised on or in an organic carrier entrapped within the carrier, e.g. gel or hollow fibres
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/10Biofuels, e.g. bio-diesel

Definitions

  • the present invention relates to a method of preparing ethanol by fermenting a lactose-containing solution with a lactase-containing microorganism.
  • alcoholic beverages by fermenting lactose, i.e. milk sugar, has been known from time immemorial. Such a fermentation allows an immediate achievement of alcohol percentages of up to 3.0%, and through distillation the alcoholic strength may be increased.
  • the article "Alkoholher ein aus MoIke” in the periodical "Die Branntwein ocean", from December 1977 discloses a method of preparing ethanol from whey.
  • a selected species of yeast Saccharomyces fragilis
  • whey permeate from an ultra-filtration plant also being added to said fermenter.
  • an overflow is established to the second fermenter, and after filling this second fermenter a draining off to a separator is initiated.
  • Part of the separated yeast float is returned to the first fermenter, whereas the wort freed from yeast is carried to a distilling plant through a buffer tank, the alcohol being continuously distilled in said plant.
  • the yeast species Saccharomyces fragilis is used in concentrations of 2 to 4 g of dry ferment per liter of fermenting wort and a lactose concentration in the whey permeate of 5 to 9% of lactose anhydrate.
  • the fermentation is carried out at a temperature of 25 to 30°C and a pH of 3.7 to 4.2.
  • this fermenting process can only proceed continuously for up to 1 week since the lactose-containing medium is easily infected with microorganisms influencing the fermentation in an undesired manner.
  • This feature especially applies to the use of Saccha romyces fragilis, which compared to the majority of other Saccharomyces species is especially sensitive to infection.
  • Saccharomyces fragilis is used by the known method for the known whey fermentation in spite of the particularly high sensitivity thereof to infection because of its capability partly of cleaving lactose and partly of fermenting both the galactose and the glucose formed by the cleaving of lactose.
  • the known method thus allows conversion velocities of lactose into ethanol of 1 to 5 ⁇ of lactose per g of dry ferment per hour.
  • the yield of the process corresponds to 75-80% of the yield theoretically obtainable, i.e. that approximately 80% of the lactose is converted into ethanol, whereas the remaining lactose is lost as a consequence of growth of yeast, side reactions and said infection.
  • the present invention relates to a method of fermenting ethanol by fermenting a lactose-containing solution with a lactase-containing microorganism, said method being characterised by using the microorganism in immobilised form.
  • the immobilisation of microorganisms is known per se and is for instance performed by encapsulating microorganisms in a polymer.
  • Polyacrylamide is one of the most used polymers, but it suffers from the disadvantage that the polymerisation is difficult to perform whilst maintaining the vitality of the immobilised microorganism.
  • the monomer used for the immobilisation is toxic.
  • the immobilisation of microorganisms by means of these substances may be carried out by initially mixing an aqueous solution of the polymer carbohydrate and the microorganisms and subsequently causing a formation of gel from the resulting mixture, e.g. through cooling or through contacting with cations such as potassium ions, ammonium ions, calcium ions, magnesium ions, stanno ions, ferri ions or aluminium ions.
  • cations such as potassium ions, ammonium ions, calcium ions, magnesium ions, stanno ions, ferri ions or aluminium ions.
  • the immobilisation may for instance be carried out by transferring the mixture of carbohydrate and microorganisms dropwise to an aqueous solution containing one of the ions causing formation of gel. As a result, guttiform solid particles containing microorganisms are obtained.
  • the invention it turned out to be possible to immobilise lactase-containing microorganisms in such a manner that the immobilised cells may be used for fermenting lactose-containing solutions.
  • the lactase-containing microorganisms through the immobilisation achieve a quite unusual resistance to infection.
  • one or more microorganisms selected among Torula cremoris, Torula sphaerica, Torula lactosa, Saccharomyces fragilis, Saccharomyces lactis, and Candida pseudotrooicalis may be used.
  • the microorganism Saccharomyces fragilis may be used for the method. It turned out surprisingly that the usually highly sensitive Saccharomyces fragilis may be immobilised by using carbohydrate-containing polymers whilst maintaining completely the vitality and capability of lactose—fermentation of the organism.
  • An immobilised lactase-containing microorganism may therefore be used for a substantially longer period by the technical method than the corresponding non-immobilised mi ⁇ roorganismn.
  • This feature is of particular importance to the fermentation of lactose-containing media, since the microorganisms used therefor are typically propagated to highest degree on a glucose-containing medium and therefore have an inducing period at the beginning of the fermentation. Thus typically 6 to 8 hours lapse from the time the microorganism is brought into contact with the lactose-containing medium, to the time the lactose fermentation occurs. This factor implies that the fermenting plant is unproductive in this period. An extension of the time of application of the microorganism therefore implies especially at lactose fermentations an increase of the productivity of the fermenting plant.
  • the lactose-containing solution is ultrafiltrated whey.
  • the fermenting is carried out by means of a single fermenter.
  • the oxygen content in the draff from the whey fermen tations as conditioned by the biochemical oxygen consumption however becomes less than usual because less residues, dead cells, are present in the fermented product.
  • a centrifugation of high liquid amounts is avoided by using immobilised yeast. This advantage is due to the above increase in productivity, which implies that the same productivity may be obtained by the method according to the invention compared to the use of the non-immobilised yeast. This is rendered possible by using a fermenting volume of about 1/5 to 1/10 of the volume used by the known technique.
  • Molasses filled in bottles is inoculated with this culture by means of a platinum needle. After two days the content of the molasses bottles is transferred into two-liter Erlenmeyer flasks containing a liter of sterile nutrient solution of the following composition: 130 g of molasses
  • the nutrient solution also used in the molasses bottles is sterilised before inoculation through autoclavering at 121oC for 30 minutes.
  • the yeast is cultured at 30°C in said molasses bottles and Erlenmeyer flasks in a shaking thermostat. After 48 hours the molasses used is decanted off, whereafter the flasks are filled with fresh molasses (nutrient solution) . After 24 hours the operation is repeated, and the following day the produced yeast is harvested.
  • the yeast is suspended in a volume of 3% of sodium alginate, and the mixture is transferred dropwise into a cold 0.1 molar solution of calcium chloride.
  • the immobilised yeast is stored therein at 3oC for 24 hours.
  • lactose-containing substrate a 9% by weight solution of lactose in water is used, and the fermentation is carried out in a thermostatically controlled fermenter provided with an overflow functioning at a volume of more than 1 liter.
  • the total volume of the fermenter is 1 1/2 liter, and 0.5 liter of immobilised yeast corresponding to about 40 g of dry ferment is filled therein.
  • the fermenting is carried out for 2 to 4 weeks whilst producing an amount of ethanol corresponding to 4.5% by volume determined through gas chromatography in the outlet of the fermenting unit.

Landscapes

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

Abstract

L'ethanol est prepare par fermentation d'une solution contenant du lactose avec un micro-organisme contenant du lactase utilise sous forme immobilisee.Ethanol is prepared by fermentation of a lactose-containing solution with a lactase-containing microorganism used in immobilized form.

Description

PREPARATION OF ETHANOLWITH IMMOBILIZED MICROORGANISM
Technical Field
The present invention relates to a method of preparing ethanol by fermenting a lactose-containing solution with a lactase-containing microorganism.
Background Art
The preparation of alcoholic beverages by fermenting lactose, i.e. milk sugar, has been known from time immemorial. Such a fermentation allows an immediate achievement of alcohol percentages of up to 3.0%, and through distillation the alcoholic strength may be increased.
Up to the Second World War the preparation of alcohol based on whey could not be economically justified. Furthermore the alcohol based on whey could not compete with the alcohol based on potatoes and molasses as raw materials.
During recent years the utilization of the lactose content of the whey for preparing ethanol has, however, gained a renewed interest as a consequence of the environmental problems arising from draining of whey in waste water. The preparation of ethanol based on whey is in the present connection to be considered an alternative to the conventional biological purification, since the sale of the ethanol processed may cover completely or partially the expenses involved in the biological purification. The development within the dairy industry, which concentrates the preparation of dairy products including cheese in still larger plants, has increased the problem concerning the removal of the whey. At the same time this development has made the preparation of ethanol from whey more attractive from an economical point of view.
The article "Alkoholherstellung aus MoIke" in the periodical "Die Branntweinwirtschaft", from December 1977 discloses a method of preparing ethanol from whey. By this method a selected species of yeast, Saccharomyces fragilis, is propagated batchwise in two steps and subsequently transferred to the first of two fermenters connected in series, whey permeate from an ultra-filtration plant also being added to said fermenter. When the first fermenter has been filled to a predetermined level, an overflow is established to the second fermenter, and after filling this second fermenter a draining off to a separator is initiated. Part of the separated yeast float is returned to the first fermenter, whereas the wort freed from yeast is carried to a distilling plant through a buffer tank, the alcohol being continuously distilled in said plant.
At the .fermentation the yeast species Saccharomyces fragilis is used in concentrations of 2 to 4 g of dry ferment per liter of fermenting wort and a lactose concentration in the whey permeate of 5 to 9% of lactose anhydrate. The fermentation is carried out at a temperature of 25 to 30°C and a pH of 3.7 to 4.2.
Typically, this fermenting process can only proceed continuously for up to 1 week since the lactose-containing medium is easily infected with microorganisms influencing the fermentation in an undesired manner. This feature especially applies to the use of Saccha romyces fragilis, which compared to the majority of other Saccharomyces species is especially sensitive to infection.
Saccharomyces fragilis is used by the known method for the known whey fermentation in spite of the particularly high sensitivity thereof to infection because of its capability partly of cleaving lactose and partly of fermenting both the galactose and the glucose formed by the cleaving of lactose.
The usual precautions against infection were to treat the yeast in question with diluted acid. This disinfection cannot, however, be employed in connection with Saccharomyces fragilis because of its general sensitivity. This sensitivity thus also makes a centrifugation unsuitable for recirculating the yeast float, which on. the contrary may be performed in connection with for instance Saccharomyces cerviciae commonly used for fermenting molasses.
The known method thus allows conversion velocities of lactose into ethanol of 1 to 5 σ of lactose per g of dry ferment per hour. The yield of the process corresponds to 75-80% of the yield theoretically obtainable, i.e. that approximately 80% of the lactose is converted into ethanol, whereas the remaining lactose is lost as a consequence of growth of yeast, side reactions and said infection. In accordance with the reaction scheme:
C12H22O11 + H2O → 4C2H5OH + 4CO2
about 42 liters of whey with a lactose content of 4.4% are thus necessary for the preparation of 1 liter of 100% ethanol at a yield of 78%. Disclosure of Invention
The present invention relates to a method of fermenting ethanol by fermenting a lactose-containing solution with a lactase-containing microorganism, said method being characterised by using the microorganism in immobilised form.
The immobilisation of microorganisms is known per se and is for instance performed by encapsulating microorganisms in a polymer. Polyacrylamide is one of the most used polymers, but it suffers from the disadvantage that the polymerisation is difficult to perform whilst maintaining the vitality of the immobilised microorganism. Furthermore the monomer used for the immobilisation is toxic.
For some time a number of polymer carbohydrates have been known to be applicable for immobilising microorganisms. Examples of carbohydrates described in this connection are K-carrageenan, -carrageenan, fur= cellaran, cellulose sulfate, alginates, and pectinates.
These substances are remarkable for their extensive use within the foodstuff industry, e.g. as a thickening agent in jam, ice, and as foaming stabilizers in beer.
The immobilisation of microorganisms by means of these substances may be carried out by initially mixing an aqueous solution of the polymer carbohydrate and the microorganisms and subsequently causing a formation of gel from the resulting mixture, e.g. through cooling or through contacting with cations such as potassium ions, ammonium ions, calcium ions, magnesium ions, stanno ions, ferri ions or aluminium ions.
The immobilisation may for instance be carried out by transferring the mixture of carbohydrate and microorganisms dropwise to an aqueous solution containing one of the ions causing formation of gel. As a result, guttiform solid particles containing microorganisms are obtained.
Previously polymeric carbohydrates were technically applied to immobilisation of Escherischia coli having aspartase activity, cf. the article "Immobilization of Escherischia coli cells having aspartase activity with carrageenan and locust bean gum", Enzyme Microb. Technol., 1979, Vol. 1, April.
The technical use of polymeric carbohydrates has , however, not previously been applied to immobilisation of lactase-containing microorganisms.
According to the invention it turned out to be possible to immobilise lactase-containing microorganisms in such a manner that the immobilised cells may be used for fermenting lactose-containing solutions. Thus it turned out that the lactase-containing microorganisms through the immobilisation achieve a quite unusual resistance to infection.
According to the invention one or more microorganisms selected among Torula cremoris, Torula sphaerica, Torula lactosa, Saccharomyces fragilis, Saccharomyces lactis, and Candida pseudotrooicalis may be used.
According to a preferred embodiment of the invention the microorganism Saccharomyces fragilis may be used for the method. It turned out surprisingly that the usually highly sensitive Saccharomyces fragilis may be immobilised by using carbohydrate-containing polymers whilst maintaining completely the vitality and capability of lactose—fermentation of the organism.
An immobilised lactase-containing microorganism may therefore be used for a substantially longer period by the technical method than the corresponding non-immobilised miσroorganismn. This feature is of particular importance to the fermentation of lactose-containing media, since the microorganisms used therefor are typically propagated to highest degree on a glucose-containing medium and therefore have an inducing period at the beginning of the fermentation. Thus typically 6 to 8 hours lapse from the time the microorganism is brought into contact with the lactose-containing medium, to the time the lactose fermentation occurs. This factor implies that the fermenting plant is unproductive in this period. An extension of the time of application of the microorganism therefore implies especially at lactose fermentations an increase of the productivity of the fermenting plant.
By the usual industrial fermenting processes on a larger scale it is therefore usually difficult to purify the used substrate sufficiently, whereby the polymer particles are often inactivated upon some time as a consequence of blocking caused by impurities.
According to a preferred embodiment of the invention, the lactose-containing solution is ultrafiltrated whey. As a result it turned out to be possible to avoid to a great extent an inactivation of the immobilising material used, and whey permeate thus proved to be particularly suited for fermenting with an immobilised microorganism, especially an immobilised species of yeast.
According to an advantageous embodiment of the invention the fermenting is carried out by means of a single fermenter.
By continuous fermentation of whey permeate it has for reaction-kinetic reasons been necessary to ferment in at least two fermenters, a lactose concentration of about 1% being maintained in the overflow between the two fenrenters. This is due to the fact that the quite particular factor applies to the lactose fermentation, that the galactose formed by the influence of the lactase on the lactose, inhibits the lactase. This particular enzyme-kinetic factor implies that in practise it has been necessary to use several fermenters connected in series in order to achieve an optimal productivity.
However, according to the invention it turned out surprisingly that fermentation of a lactose solution with immobilised lactase-containing microorganisms may be carried out in a single fermenter while maintaining the high productivity. Beyond the reduction of the fermenting volume with a factor of about 5 to 10 rendered possible by the high concentration of microorganisms in the polymer matrix used, a considerable simplification of the apparatuses necessary is thus obtained at the lactose fermentation.
By the method according to the invention it is preferred to add small amounts of air during the fermentation, preferably about 0.01 to 0.05 liter of air per liter of fermentation volume per minute.
The oxygen content in the draff from the whey fermen tations as conditioned by the biochemical oxygen consumption however becomes less than usual because less residues, dead cells, are present in the fermented product. Moreover a centrifugation of high liquid amounts is avoided by using immobilised yeast. This advantage is due to the above increase in productivity, which implies that the same productivity may be obtained by the method according to the invention compared to the use of the non-immobilised yeast. This is rendered possible by using a fermenting volume of about 1/5 to 1/10 of the volume used by the known technique.
Mode for Carrying out the Invention
Example
Preparation of ethanol through fermentation of whey permeate with immobilised Saccharomyces fragilis.
As ferment a sample of the strain Saccharomyces fragi= lis stored in test tubes on bias agar of the composition: 3 g of yeast extract 5 g of meat peptone 3 g of malt extract 10 g of glucose 20 g of agar up to 1000 ml of water, is used.
Molasses filled in bottles is inoculated with this culture by means of a platinum needle. After two days the content of the molasses bottles is transferred into two-liter Erlenmeyer flasks containing a liter of sterile nutrient solution of the following composition: 130 g of molasses
3 g of diamonium hydrogen phosphate up to 1000 ml of water, whereby the pH-value is adjusted at 4.0 by means of sulphuric acid.
The nutrient solution also used in the molasses bottles is sterilised before inoculation through autoclavering at 121ºC for 30 minutes.
The yeast is cultured at 30°C in said molasses bottles and Erlenmeyer flasks in a shaking thermostat. After 48 hours the molasses used is decanted off, whereafter the flasks are filled with fresh molasses (nutrient solution) . After 24 hours the operation is repeated, and the following day the produced yeast is harvested.
The yeast is suspended in a volume of 3% of sodium alginate, and the mixture is transferred dropwise into a cold 0.1 molar solution of calcium chloride. The immobilised yeast is stored therein at 3ºC for 24 hours.
As lactose-containing substrate, a 9% by weight solution of lactose in water is used, and the fermentation is carried out in a thermostatically controlled fermenter provided with an overflow functioning at a volume of more than 1 liter. The total volume of the fermenter is 1 1/2 liter, and 0.5 liter of immobilised yeast corresponding to about 40 g of dry ferment is filled therein.
Subsequently, 0.5 liter of 9% by weight of lactose solution is added, and the fermenting temperature is kept at 32ºC. After an adapting period of 6 to 8 hours, the fermentation starts, which is registered by means of a development of carbondioxide and a drop in the specific gravity of the fermenting solution. Subsequently, 2.5 liter of 9% by weight of lactose solution is added per hour by means of a hose pump.
The fermenting is carried out for 2 to 4 weeks whilst producing an amount of ethanol corresponding to 4.5% by volume determined through gas chromatography in the outlet of the fermenting unit.

Claims

Claims :
1. A method of preparing ethanol by fermenting a lactose-containing solution with a lactase-containing microorganism, c h a r a c t e r i s e d by the microorganism being used in immobilised form.
2. A method as .claimed in claim 1, c h a r a cte r i s e d by using as microorganism one or more selected among Torula cremoris, Torula sphaerica, Torula lactosa, Saccharomyces fragilis, Saccharomyces lactis and Candida pseudotropicalis .
3. A method as claimed in claim 2 , c h a r a cte r i s e d by the microorganism being Saccharo= myces fragilis.
4. A method as claimed in claim 1, 2 or 3, ch ar a c t e r i s e d by the microorganism being immobilised by encapsulation in a polymer.
5. A method as claimed in claim 4, c h a r a cte r i s e d by the polymer being a carbohydrate.
6. A method as claimed in claim 5 , c h a r a ct e r i s e d by the carbohydrate being selected among alginates , pectinates, carrageenans and furcellaran.
7. A method as claimed in claim 5 , c h a r a ct e r i s e d by the polymer being calcium alginate.
8. A method as claimed in any one of the preceding claims, c h a r a c t e r i s e d by the lactose-containing solution being ultra-filtrated whey.
9. A method as claimed in any one of the preceding claims, c h a r a c t e r i s e d by the fermentation being performed by use of a single fermenter.
10. A method as claimed in any of the preceding claims, c h a r a c t e r i s e d by adding small ampunts of air during the fermentation, preferably about 0.01-0.05 liter of air per liter of fermentation volume per minute.
EP81901325A 1980-05-12 1981-05-08 Preparation of ethanol with immobilized microorganism Withdrawn EP0051653A1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DK206880A DK206880A (en) 1980-05-12 1980-05-12 METHOD OF PREPARING ETHANOL
DK2068/80 1980-05-12

Publications (1)

Publication Number Publication Date
EP0051653A1 true EP0051653A1 (en) 1982-05-19

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EP81901325A Withdrawn EP0051653A1 (en) 1980-05-12 1981-05-08 Preparation of ethanol with immobilized microorganism

Country Status (5)

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EP (1) EP0051653A1 (en)
AU (1) AU7174981A (en)
DK (1) DK206880A (en)
NL (1) NL8120168A (en)
WO (1) WO1981003339A1 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4347320A (en) * 1980-11-24 1982-08-31 Miles Laboratories, Inc. Immobilization of microorganisms in gelled carrageenan
CN102660584B (en) * 2012-03-31 2014-07-16 中国海洋大学 Ethanol conversion method by utilization of marine sulfating carragheenan

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
NZ190603A (en) * 1978-06-07 1982-03-23 Nat Res Dev Heat-stable -galactosidase derived from bacillus stearothermophilus hydrolysis of lactose

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
See references of WO8103339A1 *

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NL8120168A (en) 1982-04-01
DK206880A (en) 1981-11-13
AU7174981A (en) 1981-12-07
WO1981003339A1 (en) 1981-11-26

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