DK142880B - Process for preparing alcohol from cellulose material. - Google Patents

Process for preparing alcohol from cellulose material. Download PDF

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Publication number
DK142880B
DK142880B DK111576AA DK111576A DK142880B DK 142880 B DK142880 B DK 142880B DK 111576A A DK111576A A DK 111576AA DK 111576 A DK111576 A DK 111576A DK 142880 B DK142880 B DK 142880B
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DK
Denmark
Prior art keywords
flask
cellulose material
cellulase
alcohol
flasks
Prior art date
Application number
DK111576AA
Other languages
Danish (da)
Other versions
DK142880C (en
DK111576A (en
Inventor
Shuzo Suzuki
William Frederick Gauss
Motoyashi Takagi
Original Assignee
Bio Res Ct Company 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
Priority claimed from US05/610,731 external-priority patent/US3990944A/en
Priority to CA235,874A priority Critical patent/CA1055861A/en
Priority to DE2609551A priority patent/DE2609551C2/en
Priority to GB9894/76A priority patent/GB1497958A/en
Application filed by Bio Res Ct Company Ltd filed Critical Bio Res Ct Company Ltd
Priority to DK111576AA priority patent/DK142880B/en
Priority to BE165169A priority patent/BE839573R/en
Priority to IT21315/76A priority patent/IT1064799B/en
Priority to NL7602796A priority patent/NL7602796A/en
Priority to SE7603394A priority patent/SE436756B/en
Priority to JP51029748A priority patent/JPS6043118B2/en
Priority to FI760738A priority patent/FI760738A/fi
Priority to NO760977A priority patent/NO145101C/en
Publication of DK111576A publication Critical patent/DK111576A/da
Publication of DK142880B publication Critical patent/DK142880B/en
Publication of DK142880C publication Critical patent/DK142880C/da
Application granted granted Critical

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    • 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
    • C12P7/08Ethanol, i.e. non-beverage produced as by-product or from waste or cellulosic material substrate
    • C12P7/10Ethanol, i.e. non-beverage produced as by-product or from waste or cellulosic material substrate substrate containing cellulosic material
    • 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

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  • 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)
  • Preparation Of Compounds By Using Micro-Organisms (AREA)
  • Polysaccharides And Polysaccharide Derivatives (AREA)

Description

142880 2 cellulosematerialer benytter flere trin ved først at forsukre cellulose enzymatisk med en cellulase til frembringelse af glucose, som dernæst adskilles fra det til forsukringen benyttede udgangsmateriale og særskilt underkastes et andet trin med forgæring i nærværelse af en alkoholfrembringende organisme til dannelse af alkohol.Cellulose materials utilize several steps by first enzymatically sacrificing cellulose with a cellulase to produce glucose, which is then separated from the starting material used for suction, and separately subjected to a second step of fermentation in the presence of an alcohol-producing organism to form alcohol.

Den foreliggende fremgangsmåde udgør en forbedring i forhold til fremgangsmåden ifølge hovedpatentet ved at tilvejebringe en yderligere forøgelse i udbyttet af det ønskede slutprodukt, ethylalkohol.The present process represents an improvement over the process of the main patent by providing a further increase in the yield of the desired final product, ethyl alcohol.

Dette opnås ved et særligt valg af den ene enzymkilde, nemlig cellula-sen, som benyttes ved fremgangsmåden ifølge hovedpatentet.This is achieved by a particular choice of the one enzyme source, namely the cellulase, which is used in the process of the main patent.

I overensstemmelse hermed angår den foreliggende opfindelse en fremgangsmåde ifølge patent nr. 140764 til fremstilling af alkohol, hvilken fremgangsmåde er ejendommelig ved, at man som cellulase-kilden benytter hele den vandige næringskultur hidrørende fra dyrkningen af en cellulolytisk mikroorganisme i et vandigt næringsmedium i nærværelse af et cellulosemateriale, uden adskillelse af nogen komponent fra denne næringskultur.Accordingly, the present invention relates to a process according to Patent No. 140764 for the production of alcohol which is characterized in that as the source of cellulase the whole aqueous nutritional culture derived from the cultivation of a cellulolytic microorganism in an aqueous nutrient medium is used in the presence of a cellulose material, without separating any component from this nutritional culture.

Fremgangsmåden ifølge den foreliggende opfindelse og den herved i forhold til fremgangsmåden ifølge hovedpatentet opnåede yderligere forbedring belyses tydeligere ved følgende eksempel.The process of the present invention and the further improvement thus obtained in relation to the method of the main patent are illustrated more clearly by the following example.

Eksempel I to særskilte rystekolber dyrkes Trichoderma viride QM 9414 (ATCC 26.921) aerobt ved 30°C i et tidsrum på 6 dage. Hver kolbe indeholder 100 ml af et identisk konventionelt næringsmedium, der indeholder cellulosepulver som carbonkilden. Under dyrkningen indstilles pH to gange om dagen på 5,4. Ved afslutningen af 6 dages perioden filtreres indholdet af den ene af kolberne (A) til frembringelse af et kulturfiltrat indeholdende cellulaseenzymkomplekset. Indholdet af den anden kolbe (B) filtreres ikke. Begge de således frembragte cellulaseholdige materialer benyttes ved fremgangsmåden ifølge hovedpatentet, således som nedenfor beskrevet.Example In two separate shake flasks, Trichoderma viride QM 9414 (ATCC 26.921) is grown aerobically at 30 ° C for a period of 6 days. Each flask contains 100 ml of an identical conventional nutrient medium containing cellulose powder as the carbon source. During cultivation, the pH is adjusted to 5.4 twice a day. At the end of the 6 day period, the contents of one of the flasks (A) are filtered to produce a culture filtrate containing the cellulase enzyme complex. The contents of the second flask (B) are not filtered. Both of the cellulase-containing materials thus produced are used in the process of the main patent, as described below.

I to steriliserede 100 ml kolber anbringes aseptisk og hver for sig 5 g steriliseret cellulosepulver (300 mesh, indeholdende 95 vægtprocent cellulose). I den ene af disse kolber (C) tilsættes 45 ml af ovennævnte kulturfiltrat fra kolben (A). I den anden af disse kolber (D) tilsættes 45 ml af den ovenfor omtalte grundigt omrørte, men ufiltrerede næringskultur fra kolben (B), det vil altså sige hele den vandige kul- 142880 3 tunnasse uden adskillelse af nogen komponenter derfra (det vil altså sige hele næringskultursuppen). Dernæst tilsættes til hver af kolberne (C) og (D) 5 ml af en steriliseret opløsning indeholdende følgende bestanddele :In two sterilized 100 ml flasks, aseptically and separately 5 g of sterilized cellulose powder (300 mesh containing 95% by weight of cellulose) is placed separately. To one of these flasks (C), add 45 ml of the above culture filtrate from flask (A). In the second of these flasks (D), 45 ml of the above-mentioned well-stirred but unfiltered nutritional culture from the flask (B) is added, that is, the entire aqueous coal tunnel without separating any components therefrom (i.e. say the whole nutritional culture soup). Next, add to each of flasks (C) and (D) 5 ml of a sterilized solution containing the following ingredients:

Asparagin 125 mg.Asparagine 125 mg.

KH2P04 50 mg.KH2PO4 50 mg.

MgS04 . 7H20 150 mg.MgS04. 7H 2 O 150 mg.

Gærekstrakt 10 mg.Yeast extract 10 mg.

Destilleret vand 5 mg.Distilled water 5 mg.

De herved fremkomne blandinger i hver kolbe indstilles på pH 4,0 efter behov. Derefter tilsættes 2 platinøjefulde af saccharo-myces cerevisiae direkte fra en skråagar deraf til hver af kolberne, og blandingen tillades at omsættes anaerobt ved ca. 30°C i 96 timer.The resulting mixtures in each flask are adjusted to pH 4.0 as needed. Then, 2 platinum eyes of Saccharomyces cerevisiae are added directly from one oblique agar thereof to each of the flasks, and the mixture is allowed to react anaerobically at ca. 30 ° C for 96 hours.

Når reaktionsblandingerne analyseres, konstateres dannelse af 1,2 g ethanol i blandingen fra kolben (C), hvorimod der iagttages dannelsen af 1,4 g ethanol i blandingen fra kolben (D). Når omsætningen fortsættes i yderligere 96 timer, viser det sig, at blandingen fra kolben (C) indeholder 2,0 g ethanol, medens blandingen fra kolben (D) indeholder 2,3 g ethanol.When analyzing the reaction mixtures, formation of 1.2 g of ethanol in the mixture from the flask (C) is observed, whereas the formation of 1.4 g of ethanol in the mixture from the flask (D) is observed. When the reaction is continued for an additional 96 hours, it appears that the mixture from the flask (C) contains 2.0 g of ethanol, while the mixture from the flask (D) contains 2.3 g of ethanol.

En sammenligning af de således opnåede resultater viser, , at man ved brugen af hele kulturmediet (kolben (B)) som cellulase- kilden sammenlignet med resultater opnået ved brug af kulturfiltratet (kolben (C)) som cellulasekilden opnår en bemærkelsesværdig forbedring i udbyttet af ethanol, nemlig 2,3 g sammenlignet med 2,0 g, hvilket indicerer en forøgelse på 15% i udbyttet af ønsket produkt, ethylal-kohol.A comparison of the results thus obtained shows that by using the entire culture medium (flask (B)) as the source of cellulase compared with results obtained using the culture filtrate (flask (C)) as the source of cellulase, a remarkable improvement in the yield of ethanol, namely 2.3 g compared to 2.0 g, indicating a 15% increase in the yield of desired product, ethyl alcohol.

Claims (1)

4 Ι420βϋ Patentkrav. Fremgangsmåde ifølge patent nr. 140764 til fremstilling af alkohol ud fra cellulosemateriale, kendetegnet ved, at man som cellulasekilden anvender hele den vandige næringskultur, der fås ved dyrkning af en cellulolytisk mikroorganisme i et vandigt næringsmedium i nærværelse af et cellulosemateriale, uden adskillelse af nogen komponent derfra. Fremdragne publikationer: Langkj»r København '9 <· ;i4 Ι420βϋ Patent Claims. Process according to patent 140764 for the production of alcohol from cellulose material, characterized in that as the cellulase source, the whole aqueous nutrient culture obtained by growing a cellulolytic microorganism in an aqueous nutrient medium in the presence of a cellulosic material is used, without separating any component. from there. Published publications: Langkj »r Copenhagen '9 <·; i
DK111576AA 1974-09-20 1976-03-15 Process for preparing alcohol from cellulose material. DK142880B (en)

Priority Applications (11)

Application Number Priority Date Filing Date Title
CA235,874A CA1055861A (en) 1974-09-20 1975-09-19 Manufacture of alcohol from cellulosic materials
DE2609551A DE2609551C2 (en) 1975-09-08 1976-03-08 Production of alcohol from cellulose
GB9894/76A GB1497958A (en) 1975-09-08 1976-03-12 Manufacture of ethanol from cellulosic materials
DK111576AA DK142880B (en) 1975-09-08 1976-03-15 Process for preparing alcohol from cellulose material.
BE165169A BE839573R (en) 1975-09-08 1976-03-15 MANUFACTURE OF ALCOHOL FROM CELLULOSIC MATERIALS
NL7602796A NL7602796A (en) 1975-09-08 1976-03-17 PROCESS FOR PREPARING ALCOHOL FROM CELL LULOSE MATERIAL.
IT21315/76A IT1064799B (en) 1975-09-08 1976-03-17 PROCEDURE FOR THE PRODUCTION OF ALCOHOL WITH HIGH YIELDS FROM CELLULOSE MATERIALS
SE7603394A SE436756B (en) 1975-09-08 1976-03-18 SEE IN THE MANUFACTURE OF ETHANOL FROM CELLULOSAMATERIAL THROUGH THE IMPACT OF CELLULAS AND AN ALCOHOL PRODUCING MICROORGANISM
JP51029748A JPS6043118B2 (en) 1975-09-08 1976-03-18 How to make alcohol from cellulose
FI760738A FI760738A (en) 1975-09-08 1976-03-19
NO760977A NO145101C (en) 1975-09-08 1976-03-19 PROCEDURE FOR THE PREPARATION OF ETHANOL FROM CELLULOSE SUBSTANCES.

Applications Claiming Priority (6)

Application Number Priority Date Filing Date Title
US61073175 1975-09-08
US05/610,731 US3990944A (en) 1974-09-20 1975-09-08 Manufacture of alcohol from cellulosic materials using plural ferments
DK422375AA DK140764B (en) 1974-09-20 1975-09-19 Process for producing alcohol from cellulosic material.
DK422375 1975-09-19
DK111576 1976-03-15
DK111576AA DK142880B (en) 1975-09-08 1976-03-15 Process for preparing alcohol from cellulose material.

Publications (3)

Publication Number Publication Date
DK111576A DK111576A (en) 1977-03-09
DK142880B true DK142880B (en) 1981-02-16
DK142880C DK142880C (en) 1981-08-31

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Family Applications (1)

Application Number Title Priority Date Filing Date
DK111576AA DK142880B (en) 1974-09-20 1976-03-15 Process for preparing alcohol from cellulose material.

Country Status (10)

Country Link
JP (1) JPS6043118B2 (en)
BE (1) BE839573R (en)
DE (1) DE2609551C2 (en)
DK (1) DK142880B (en)
FI (1) FI760738A (en)
GB (1) GB1497958A (en)
IT (1) IT1064799B (en)
NL (1) NL7602796A (en)
NO (1) NO145101C (en)
SE (1) SE436756B (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101821397A (en) * 2007-10-12 2010-09-01 丹尼斯科美国公司 From organism of fermentation, improve the method and composition that organism produces
CN102325889A (en) * 2008-12-19 2012-01-18 诺维信股份有限公司 Increase the method for cellulose materials hydrolysis

Also Published As

Publication number Publication date
DE2609551A1 (en) 1977-03-10
SE7603394L (en) 1977-03-09
DE2609551C2 (en) 1982-06-03
IT1064799B (en) 1985-02-25
NO145101B (en) 1981-10-05
JPS5234981A (en) 1977-03-17
DK142880C (en) 1981-08-31
GB1497958A (en) 1978-01-12
DK111576A (en) 1977-03-09
SE436756B (en) 1985-01-21
JPS6043118B2 (en) 1985-09-26
NL7602796A (en) 1977-03-10
NO145101C (en) 1982-01-13
BE839573R (en) 1976-09-15
FI760738A (en) 1977-03-06
NO760977L (en) 1977-03-09

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