JPS5910795B2 - Alcohol production method by fermentation - Google Patents
Alcohol production method by fermentationInfo
- Publication number
- JPS5910795B2 JPS5910795B2 JP55126771A JP12677180A JPS5910795B2 JP S5910795 B2 JPS5910795 B2 JP S5910795B2 JP 55126771 A JP55126771 A JP 55126771A JP 12677180 A JP12677180 A JP 12677180A JP S5910795 B2 JPS5910795 B2 JP S5910795B2
- Authority
- JP
- Japan
- Prior art keywords
- fermentation
- production method
- bacterial
- alcohol production
- 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
Links
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 title claims description 12
- 238000000855 fermentation Methods 0.000 title claims description 10
- 230000004151 fermentation Effects 0.000 title claims description 10
- 238000004519 manufacturing process Methods 0.000 title claims description 5
- 239000010455 vermiculite Substances 0.000 claims description 8
- 235000019354 vermiculite Nutrition 0.000 claims description 8
- 229910052902 vermiculite Inorganic materials 0.000 claims description 8
- 230000010065 bacterial adhesion Effects 0.000 claims description 4
- 230000001580 bacterial effect Effects 0.000 description 11
- 210000004027 cell Anatomy 0.000 description 10
- 241000894006 Bacteria Species 0.000 description 4
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 240000004808 Saccharomyces cerevisiae Species 0.000 description 3
- 235000014680 Saccharomyces cerevisiae Nutrition 0.000 description 3
- 238000010790 dilution Methods 0.000 description 3
- 239000012895 dilution Substances 0.000 description 3
- TWRXJAOTZQYOKJ-UHFFFAOYSA-L Magnesium chloride Chemical compound [Mg+2].[Cl-].[Cl-] TWRXJAOTZQYOKJ-UHFFFAOYSA-L 0.000 description 2
- LRHPLDYGYMQRHN-UHFFFAOYSA-N N-Butanol Chemical compound CCCCO LRHPLDYGYMQRHN-UHFFFAOYSA-N 0.000 description 2
- 229910021536 Zeolite Inorganic materials 0.000 description 2
- 241000588902 Zymomonas mobilis Species 0.000 description 2
- 238000005299 abrasion Methods 0.000 description 2
- 238000005273 aeration Methods 0.000 description 2
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 2
- JVTAAEKCZFNVCJ-UHFFFAOYSA-N lactic acid Chemical compound CC(O)C(O)=O JVTAAEKCZFNVCJ-UHFFFAOYSA-N 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 229920001296 polysiloxane Polymers 0.000 description 2
- 239000004576 sand Substances 0.000 description 2
- 239000010457 zeolite Substances 0.000 description 2
- NLXLAEXVIDQMFP-UHFFFAOYSA-N Ammonia chloride Chemical compound [NH4+].[Cl-] NLXLAEXVIDQMFP-UHFFFAOYSA-N 0.000 description 1
- WQZGKKKJIJFFOK-GASJEMHNSA-N Glucose Natural products OC[C@H]1OC(O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-GASJEMHNSA-N 0.000 description 1
- 244000017020 Ipomoea batatas Species 0.000 description 1
- 235000002678 Ipomoea batatas Nutrition 0.000 description 1
- 241000108056 Monas Species 0.000 description 1
- 240000000111 Saccharum officinarum Species 0.000 description 1
- 235000007201 Saccharum officinarum Nutrition 0.000 description 1
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 1
- 244000061456 Solanum tuberosum Species 0.000 description 1
- 235000002595 Solanum tuberosum Nutrition 0.000 description 1
- 240000008042 Zea mays Species 0.000 description 1
- 235000005824 Zea mays ssp. parviglumis Nutrition 0.000 description 1
- 235000002017 Zea mays subsp mays Nutrition 0.000 description 1
- 235000019270 ammonium chloride Nutrition 0.000 description 1
- 239000002518 antifoaming agent Substances 0.000 description 1
- 229940041514 candida albicans extract Drugs 0.000 description 1
- 230000010261 cell growth Effects 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 235000005822 corn Nutrition 0.000 description 1
- 238000012136 culture method Methods 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 239000008103 glucose Substances 0.000 description 1
- 125000002791 glucosyl group Chemical group C1([C@H](O)[C@@H](O)[C@H](O)[C@H](O1)CO)* 0.000 description 1
- 150000004676 glycans Chemical class 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 210000001822 immobilized cell Anatomy 0.000 description 1
- 235000014655 lactic acid Nutrition 0.000 description 1
- 239000004310 lactic acid Substances 0.000 description 1
- 229910001629 magnesium chloride Inorganic materials 0.000 description 1
- 230000000813 microbial effect Effects 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 235000013379 molasses Nutrition 0.000 description 1
- 239000003348 petrochemical agent Substances 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 229920001282 polysaccharide Polymers 0.000 description 1
- 239000005017 polysaccharide Substances 0.000 description 1
- 235000012015 potatoes Nutrition 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 241000894007 species Species 0.000 description 1
- 239000004575 stone Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000012138 yeast extract Substances 0.000 description 1
Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/10—Biofuels, e.g. bio-diesel
Landscapes
- Preparation Of Compounds By Using Micro-Organisms (AREA)
Description
【発明の詳細な説明】
本発明は醗酵によるアルコール製造法に関する.近年石
油代替エネルギーとして、石油化学によらずに得られる
醗酵アルコールが脚光を浴びている。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing alcohol by fermentation. In recent years, fermented alcohol, which can be obtained without using petrochemicals, has been in the spotlight as an energy alternative to petroleum.
これはさとうきびやこれから採っだ糖蜜、さつまいも、
じゃがいも、とうもろこし等のセルロース質ないしはで
ん粉質を原料とし、これらを菌体の作用によって醗酵さ
せて製造される。This is sugar cane, molasses, sweet potato,
It is produced by fermenting cellulosic or starchy materials such as potatoes and corn through the action of bacterial cells.
この方法では、アルコールの生産性は菌体濃度に依存す
ると考えられている。In this method, alcohol productivity is thought to depend on the bacterial cell concentration.
そのため菌体濃度を高めるために、菌体を循環させる方
法や、酵母を多糖系物質中に包括させるいわゆる固定化
増殖菌体法等が開発されつつある。Therefore, in order to increase the bacterial cell concentration, a method of circulating the bacterial cells and a so-called immobilized cell growth method in which yeast is encapsulated in a polysaccharide-based substance are being developed.
しかし前者の場合、菌体を濃縮分離するのに用いる遠心
分離器が、培養液中に存在する固形物によって目詰まり
ないしはノズル詰まりをきたし、菌体の循環が次第に困
難になる。However, in the former case, the centrifugal separator used to concentrate and separate the bacterial cells becomes clogged or nozzles clogged by the solids present in the culture solution, making it increasingly difficult to circulate the bacterial cells.
そのため遠心分離器を定期的に洗浄してやる必要があり
、作業がはなはだ面倒になる。Therefore, it is necessary to periodically clean the centrifuge, which makes the work extremely troublesome.
また後者の場合には、工業的規模で大量生産するには、
技術的に解決困難な問題が多い。In the latter case, for mass production on an industrial scale,
There are many problems that are technically difficult to solve.
本発明者はこのような実隋に鑑み、醗酵槽内の菌体濃度
を高めるべく鋭意研究を重ねた結果、本発明を完成する
に至った。In view of these circumstances, the present inventor has conducted extensive research to increase the concentration of microbial cells in the fermenter, and as a result has completed the present invention.
すなわち、本発明は、醗酵槽内における菌体付着用の媒
体として粉砕した多孔質のヒル石を用いたことを特徴と
する醗酵によるアルコール製造法である。That is, the present invention is a method for producing alcohol by fermentation, which is characterized by using crushed porous vermiculite as a medium for bacterial cell attachment in a fermentation tank.
菌体付着用の媒体としては、粉砕した多孔質のヒル石の
ほかに、たとえば砂、活性炭、ゼオライト等も考えられ
るので、これらについても検討した。In addition to crushed porous vermiculite, sand, activated carbon, zeolite, and the like may be used as a medium for bacterial adhesion, and these were also considered.
その結果はつぎのとおりである。すなわち砂の場合、分
散性が悪くてこれを均一分散させるのに大きな動力を要
する。The results are as follows. In other words, sand has poor dispersibility and requires a large amount of power to uniformly disperse it.
また活性炭およびゼオライトの場合、強度が劣るため機
械的分散による摩耗が著しい。Furthermore, in the case of activated carbon and zeolite, their strength is inferior, so they are subject to significant wear due to mechanical dispersion.
これに対し、粉砕した多孔質のヒル石は分散性に富みか
つ耐摩耗性に優れたものであって、菌体付着用の媒体と
しては最適である。On the other hand, crushed porous vermiculite is highly dispersible and has excellent abrasion resistance, making it optimal as a medium for bacterial adhesion.
粉砕した多孔質のヒル石としては、原石を熱処理等によ
り脱水し、ついで粉砕することにより形成したものがよ
く使用されるが、これに限定されるものではない。As the porous crushed vermiculite, one formed by dehydrating raw stone by heat treatment or the like and then crushing it is often used, but it is not limited thereto.
この粉砕物は超薄片をなすために分散性がよく、また耐
摩耗性にも優れており、しかも比表面積も大きくて、そ
のため菌体を多量に付着させることができる。This pulverized material has excellent dispersibility and abrasion resistance because it forms ultra-thin flakes, and also has a large specific surface area, so that a large amount of bacterial cells can be attached thereto.
実施例
供試菌株としてサツカロミセス・セレビシエ・スピーシ
ズ(S accharomyces cerevisi
ae spec−ies )を用い、菌体付着用の媒体
として60〜80メッシュに粉砕した多孔質のヒル石を
用い、醗酵槽内に菌株と支持体10wt/v%を投入し
た。As a sample strain of Example, Saccharomyces cerevisiae sp.
AE spec-ies), porous vermiculite crushed to 60 to 80 mesh was used as a medium for bacterial cell attachment, and 10 wt/v% of the bacterial strain and support were introduced into a fermentation tank.
なお、醗酵槽としては、ヒル石の粉砕物を分離する目的
で、沈降部を付設したものか、または槽内上部に分離手
段を設けたものを使用した。The fermentation tank used was one equipped with a sedimentation section or a separation means provided at the upper part of the tank for the purpose of separating the crushed vermiculite.
培地の組成は、グルコース1 5 0 f/ム酵母エキ
ス3.0?/t,NH4Cl 2.0f/l,KH2P
O40.8f/t,MgCl2・6H20 0.2?/
tおよびCaCl20.1であシ、この培地にはさらに
消泡剤としてシリコーン(東芝シリコーン)0.1?/
1を添加した。The composition of the medium is glucose 150 f/mu yeast extract 3.0? /t, NH4Cl 2.0f/l, KH2P
O40.8f/t, MgCl2・6H20 0.2? /
t and CaCl20.1, and this medium also contains silicone (Toshiba Silicone) 0.1?2 as an antifoaming agent. /
1 was added.
醗酵条件は、pH=5、温度=30℃、通気量=0.0
2〜0. 1 vvm程度、希釈率=0.2/時とした
。Fermentation conditions were pH=5, temperature=30℃, and aeration rate=0.0.
2-0. The dilution rate was approximately 1 vvm and the dilution rate was 0.2/hour.
この条件下に連結培養を行ない、エタノールを生産性1
4f/l・時で取得した。Continuous culture was carried out under these conditions, and ethanol was produced at a productivity of 1
Obtained at 4f/l·hr.
また供試菌株としてザイモモナス・モビリス(Zymo
monas mobilis ) I FO/ 3 7
5 6を用いて、上記操作を繰返した。In addition, Zymomonas mobilis (Zymomonas mobilis) was used as a test bacterial strain.
monas mobilis) IFO/ 3 7
The above operation was repeated using 56.
ただし醗酵条件は、pH=4、無通気下、希釈率0.5
7時とした。However, the fermentation conditions are pH = 4, no aeration, dilution rate 0.5.
It was set at 7 o'clock.
その結果、エタノールの生産性は約3 5 fi−/,
l・時であった。As a result, the productivity of ethanol is approximately 3 5 fi-/,
It was l.
このようにバクテリアの場合、酵母に比べて生産性が大
幅に向上した。In this way, the productivity of bacteria has been significantly improved compared to yeast.
その理由はバクテリアが比較的小さいために、多孔質の
ヒル石内に付着して大量に増殖したためと考えられる。The reason for this is thought to be that bacteria are relatively small, so they adhered to the porous vermiculite and multiplied in large quantities.
さらに乳酸菌やブタノール菌等についても上記と同様に
操作したが、いずれの場合も生産性が大幅に向上した。Furthermore, the same procedure as above was performed for lactic acid bacteria, butanol bacteria, etc., and the productivity was significantly improved in all cases.
これに対し、菌体付着用媒体を用いない基本的な連続培
養法では、エタノールの生産性は2〜3?/t・時であ
ると報告されている。On the other hand, in the basic continuous culture method that does not use a medium for bacterial adhesion, the ethanol productivity is 2 to 3? /t hours.
このように、本発明によれば、生産性を大幅に向上させ
ることができる。Thus, according to the present invention, productivity can be significantly improved.
Claims (1)
多孔質のヒル石を用いたことを特徴とする醗酵によるア
ルコール製造法。1. A method for producing alcohol by fermentation, characterized in that porous crushed vermiculite is used as a medium for bacterial adhesion in a fermentation tank.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP55126771A JPS5910795B2 (en) | 1980-09-11 | 1980-09-11 | Alcohol production method by fermentation |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP55126771A JPS5910795B2 (en) | 1980-09-11 | 1980-09-11 | Alcohol production method by fermentation |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS5750888A JPS5750888A (en) | 1982-03-25 |
JPS5910795B2 true JPS5910795B2 (en) | 1984-03-12 |
Family
ID=14943513
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP55126771A Expired JPS5910795B2 (en) | 1980-09-11 | 1980-09-11 | Alcohol production method by fermentation |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5910795B2 (en) |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5876096A (en) * | 1981-10-31 | 1983-05-09 | Mitsubishi Kakoki Kaisha Ltd | Continuous alcohol fermentation process |
US4504582A (en) * | 1982-07-20 | 1985-03-12 | Genex Corporation | Vermiculite as a carrier support for immobilized biological materials |
JPS59196095A (en) * | 1983-04-22 | 1984-11-07 | Hitachi Zosen Corp | Alcohol production method by fermentation |
RU2094459C1 (en) * | 1991-04-22 | 1997-10-27 | Кемира Ой | Method of fermentation on solid cultural medium |
-
1980
- 1980-09-11 JP JP55126771A patent/JPS5910795B2/en not_active Expired
Also Published As
Publication number | Publication date |
---|---|
JPS5750888A (en) | 1982-03-25 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
Suresh et al. | Utilization of damaged sorghum and rice grains for ethanol production by simultaneous saccharification and fermentation | |
ES2166316A1 (en) | PROCEDURE FOR THE PRODUCTION OF ETHANOL FROM LIGNOCELLULOSIC BIOMASS USING A NEW THERMOTOLERANT YEAST. | |
FR2477572A1 (en) | PROCESS FOR PRODUCING ETHANOL COMPRISING THE CULTURE OF A SPECIFIC MOBILIS ZYMOMONAS STRAIN AND ETHANOL PRODUCED THEREBY | |
JP4038577B2 (en) | Alcohol production system and alcohol production method | |
WO2008040358A1 (en) | A method for providing proteins and fermentation products from a plant material | |
Sree et al. | High alcohol production by solid substrate fermentation from starchy substrates using thermotolerant Saccharomyces cerevisiae | |
JPS5910795B2 (en) | Alcohol production method by fermentation | |
JP5845484B2 (en) | Novel yeast and method for producing ethanol using the same | |
Panchal et al. | Ethanol production by genetically modified strains of Saccharomyces | |
CN100569946C (en) | The separation of candida tropicalis bacterial strain and be used for the method that Xylitol is produced | |
Archibong et al. | Ethanol production from cassava wastes (pulp and peel) using alcohol tolerant yeast isolated from palm wine | |
JPH0358715B2 (en) | ||
JPS6342690A (en) | Production of ethanol by yeast fermentative at high temperature | |
JP6123504B2 (en) | Ethanol production method | |
Patil et al. | Novel supplements enhance the ethanol production in cane molasses fermentation by recycling yeast cell | |
JPS61139395A (en) | Production of ethanol | |
JPS58129983A (en) | Continuous alcohol production method using mixed culture | |
JPS6136920B2 (en) | ||
CN118580990B (en) | Clostridium tyrobutyricum TGL-A236 and method for producing fatty acids by fermenting stem juice | |
JPH0121957B2 (en) | ||
JPS6135835B2 (en) | ||
JPS6135834B2 (en) | ||
JPS6359884A (en) | Method and apparatus for producing enzymes and methane from organic waste by fermentation method | |
Margaritis et al. | Fermentation of polyfructans to ethanol by Saccharomyces rosei | |
JPS58129986A (en) | Continuous preparation of alcohol by fermentation |