JPS58129980A - Continuous preparation of alcohol by fluidizing immobilized microbial cell - Google Patents

Continuous preparation of alcohol by fluidizing immobilized microbial cell

Info

Publication number
JPS58129980A
JPS58129980A JP57011291A JP1129182A JPS58129980A JP S58129980 A JPS58129980 A JP S58129980A JP 57011291 A JP57011291 A JP 57011291A JP 1129182 A JP1129182 A JP 1129182A JP S58129980 A JPS58129980 A JP S58129980A
Authority
JP
Japan
Prior art keywords
tank
alcohol
fermentation
carrier
immobilized microbial
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.)
Pending
Application number
JP57011291A
Other languages
Japanese (ja)
Inventor
Kenji Kida
建次 木田
Shigeru Morimura
茂 森村
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.)
Hitachi Zosen Corp
Original Assignee
Hitachi Zosen Corp
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 Hitachi Zosen Corp filed Critical Hitachi Zosen Corp
Priority to JP57011291A priority Critical patent/JPS58129980A/en
Publication of JPS58129980A publication Critical patent/JPS58129980A/en
Pending legal-status Critical Current

Links

Classifications

    • 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

Abstract

PURPOSE:To increase the concentration of microbial cells in the tank, in the titled process for the continuous preparation of alcohol, and to improve the productivity of alcohol, by using a fermentor furnished with a means for separating the carrier from the reaction liquid. CONSTITUTION:The fermentor 1 is composed of a fermentation tank 3 having a stirrer 2 and a carrier precipitation chamber 4 at the side of the fermentar to precipitate and collect the immobilized microbial cells and prevent the escape of the cells from the tank. As an alternative arrangement, the fermentor 11 is composed of the fermentation tank 13 and a carrier precipitation tank 14 placed separately from the fermentation tank 13, and the reaction liquid is circulated between the tank 13 and the precipitation tank 14. The immobilized microbial cell is, e.g. Zymomonas mobilis supported on pulverized vermiculite.

Description

【発明の詳細な説明】 本発明は付着菌体流動法によるアルコールの連続製造法
に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for continuous production of alcohol using an attached bacterial cell flow method.

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。これはさと
うきびやこれから採った糖蜜、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。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。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。し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。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。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 recent years, fermented alcohol, which can be obtained without using petrochemicals, has been in the spotlight as an energy alternative to petroleum. It is produced by fermenting sugar cane, molasses, sweet potatoes, potatoes, corn, and other cellulose or starch materials through the action of bacterial cells. In this method, alcohol productivity is thought to depend on the bacterial cell concentration. 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. As a result, clogging or nozzle clogging occurs, and circulation of bacterial cells becomes increasingly difficult. Therefore, it is necessary to periodically clean the centrifuge, which makes the work extremely troublesome. In the latter case, there are many technical problems that are difficult to solve in mass production on an industrial scale.

本発明者らは、このような実情に鑑み、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 inventors of the present invention have conducted extensive research to increase the concentration of bacterial cells in the fermenter, and as a result, have completed the present invention.

この発明によるアルコールの製造法は、反応液から担体
を分離する分離手段を備えた醗酵装置を用い、担体に付
着した菌体を流動化させることを特徴とする付着菌体流
動法によるアルコールの連続製造法である。
The method for producing alcohol according to the present invention uses a fermentation device equipped with a separation means for separating the carrier from the reaction solution, and the continuous production of alcohol by the adhered bacterial cell fluidization method, which is characterized by fluidizing the bacterial cells attached to the carrier. It is a manufacturing method.

分離手段を備えた醗酵装置の例としては、添付図面に示
すようなものが挙げられる。すなわち第1図(イjに示
す醗酵装置(1)は、撹拌機(2)を備えた醗酵槽(3
)の側部に担体沈降部(4)を設け、回部+41に担体
を沈降分離させて同槽外への流出を防ぐようにしたもの
である。また第1図(ロ)に示す醗酵装置(11)は、
撹拌機[2を備えた醗酵槽t131の外部に担体沈降槽
圓を設けて、醗酵槽(13Iから流出した担体を沈降槽
(141内に沈降分離させ、沈降した担体を醗酵槽(1
31へ戻すようにしたものである。また第1図(/jに
示す醗酵装置r21)は、醗酵槽■3)の槽底部に撹拌
翼■を配置し、翼の」ニガに垂直に円筒状の液循環部材
(241を配置して、反応液を同部材例内を流下させて
槽内を循環させ、液循環部材例の上方で、担体を反応液
から分離するようにしたものである。さらに第1図に)
)に示す醗酵装置C(11は、撹拌機@を備えた醗酵槽
缶内ものである。そしてこれら醗酵装置tll’121
11311 MはいずれもpHおよび温度を至適値に制
御できるように構成されている。
Examples of fermentation devices equipped with separation means include those shown in the accompanying drawings. In other words, the fermentation apparatus (1) shown in FIG.
A carrier sedimentation section (4) is provided on the side of the tank, and the carrier is sedimented and separated in the circulation section +41 to prevent it from flowing out of the tank. In addition, the fermentation device (11) shown in Figure 1 (b) is
A carrier sedimentation tank ring is provided outside the fermentation tank t131 equipped with a stirrer [2], and the carriers flowing out from the fermentation tank (13I) are separated by sedimentation in the sedimentation tank (141), and the sedimented carriers are separated in the fermentation tank (141).
31. In addition, the fermentation device r21 shown in FIG. , the reaction liquid is allowed to flow down through the member and circulated within the tank, and the carrier is separated from the reaction liquid above the liquid circulation member.
) The fermentation device C shown in (11 is a fermentation tank can equipped with an agitator @) and these fermentation devices tll'121
11311M are all configured so that pH and temperature can be controlled to optimal values.

萌体付着用の担体は、耐摩耗性および流動性のよい小径
粒体であればよく、最適例としては粉砕ヒル石が挙げら
れる。担体はセラミック製いられる。アルコール醗酵能
を有する細菌は、倉巷自然付着性のよいものであれば、
上記細菌に限定されない。こうして醗酵槽内で担体付着
流 菌体を撹拌によって流動化させることにより、槽内の菌
体濃度を高めて、醗酵性糖からのアルコールの生産性を
向上させることができる。
The carrier for adhering sprouts may be small-diameter particles with good abrasion resistance and fluidity, and the most suitable example is crushed vermiculite. The carrier is made of ceramic. Bacteria that have alcohol fermentation ability are those that have good natural adhesion,
It is not limited to the above bacteria. By fluidizing the carrier-adhered bacterial cells in the fermentation tank by stirring, the concentration of bacterial cells in the tank can be increased and the productivity of alcohol from fermentable sugar can be improved.

実施例 第1N−)に示す醗酵装置を用いた。Example The fermentation apparatus shown in No. 1N-) was used.

まずこの醗酵装置の内部を約10容量チのエタノール液
で洗浄しておく。そして グルコース       150 f/を酵母エキス 
      39/l KH2PO41F/J (NH4)2SO4l5le/ MgC1!2・6 H200,5V/1消泡剤 (来夏
シリコン社製)  0.3fl/1からなる培地を調製
し、これに加熱処理した粉砕ヒル石(60〜80メツシ
ユ)を5 w L、/vowチになるように加え、上記
培地を加熱滅菌処理した。そして上記担体含有培地にお
いて培養したサイモモナス・モービリスATCC寄託第
10988号の培養液21!を醗酵装置に充填し、pH
を4.5に温度を30℃それぞれに制御して、醗酵原料
として上記滅菌済の培地をマイクロポンプで流量0.0
6f/bで醗酵装置に連続供給して、連続醗酵を行なっ
た。
First, the inside of this fermentation apparatus is cleaned with approximately 10 volumes of ethanol solution. and glucose 150 f/yeast extract
39/l KH2PO41F/J (NH4)2SO4l5le/ MgC1!2.6 H200,5V/1 antifoaming agent (manufactured by Next Summer Silicon Co., Ltd.) A culture medium consisting of 0.3 fl/1 was prepared, and this was heat-treated with crushed leeches. Stones (60 to 80 mesh) were added at 5 wL/vow, and the medium was heat sterilized. And culture solution 21 of Thymomonas mobilis ATCC Deposit No. 10988 cultured in the above carrier-containing medium! Fill the fermentation equipment and adjust the pH
The temperature was controlled at 4.5°C and 30°C, and the sterilized medium was used as a fermentation raw material at a flow rate of 0.0 using a micro pump.
Continuous fermentation was carried out by continuously supplying the mixture to a fermentation apparatus at 6 f/b.

つぎに原料供給流量を段階的に上げて、各流量における
エタノール濃度を測定した。原料希釈率(−原料供給流
量/磨酵槽全実容#)とアルコール生産性および醗酵収
率の関係を第2図に示す。同図かられかるかうに、アル
コール生産性は希釈率の増加に伴って増加し、希釈率0
3hlではアルコール生産性は約179/l@b。
Next, the raw material supply flow rate was increased stepwise, and the ethanol concentration at each flow rate was measured. FIG. 2 shows the relationship between the raw material dilution rate (-raw material supply flow rate/total fermentation tank actual volume #), alcohol productivity, and fermentation yield. As can be clearly seen from the figure, alcohol productivity increases as the dilution rate increases, and
At 3 hl, alcohol productivity is approximately 179/l@b.

またアルコール、醗酵収率は90%という高い値となっ
た。これに対し、菌体付着用担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2〜39/l・h
であると報告されている。このように、本発明によれば
、アルコールの生産性を大幅に向上させることができる
Furthermore, the alcohol and fermentation yields were as high as 90%. On the other hand, in the basic continuous culture method that does not use carriers for bacterial attachment, the ethanol productivity is 2 to 39/l/h.
It is reported that. As described above, according to the present invention, alcohol productivity can be significantly improved.

第1図7はこの発明の実施例を示す醗酵装置の概略図、
第2図は実施例における原料希釈率とアルコール生産性
および醗酵収率の関係を示すグラフである。
FIG. 17 is a schematic diagram of a fermentation apparatus showing an embodiment of the present invention;
FIG. 2 is a graph showing the relationship between raw material dilution rate, alcohol productivity, and fermentation yield in Examples.

fil Cl1l f211 t311−’−・醗酵装
置、t2+ [121:V 11@@撹拌機、@・・・
撹拌翼、f3N13B!31((31””醗酵槽、14
+1111@沈降部、α勾・・・沈降槽、―・・・液循
環部材、(財)・・・固液分離部材。
fil Cl1l f211 t311-'-・Fermentation device, t2+ [121:V 11@@Stirrer, @...
Stirring blade, f3N13B! 31 ((31"" fermenter, 14
+1111@Sedimentation section, α gradient...Sedimentation tank, ---Liquid circulation member, Foundation...Solid-liquid separation member.

以  上 特許出願人  日立造船株式会社 外4名 、 第2図 4帆午 (h ) −a−訣醒販峯 ベー生14生that's all Patent applicant: Hitachi Zosen Corporation 4 other people , Figure 2 4 hours (h) -a-Keisenhanmine 14th grade student

Claims (1)

【特許請求の範囲】[Claims] 反応液から担体を分離する分離手段を備えたmt4装置
を用い、担体に付着した菌体を流動化させることを特徴
とする付着菌体流動法によるアルコールの連続製造法。
1. A method for continuous production of alcohol by an adhered bacterial cell fluidization method, characterized in that bacterial cells adhering to a carrier are fluidized using an mt4 apparatus equipped with a separation means for separating the carrier from a reaction solution.
JP57011291A 1982-01-26 1982-01-26 Continuous preparation of alcohol by fluidizing immobilized microbial cell Pending JPS58129980A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57011291A JPS58129980A (en) 1982-01-26 1982-01-26 Continuous preparation of alcohol by fluidizing immobilized microbial cell

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57011291A JPS58129980A (en) 1982-01-26 1982-01-26 Continuous preparation of alcohol by fluidizing immobilized microbial cell

Publications (1)

Publication Number Publication Date
JPS58129980A true JPS58129980A (en) 1983-08-03

Family

ID=11773888

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57011291A Pending JPS58129980A (en) 1982-01-26 1982-01-26 Continuous preparation of alcohol by fluidizing immobilized microbial cell

Country Status (1)

Country Link
JP (1) JPS58129980A (en)

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