JPS60244294A - Process for semicontinuous production of alcohol in high concentration from cellulose - Google Patents
Process for semicontinuous production of alcohol in high concentration from celluloseInfo
- Publication number
- JPS60244294A JPS60244294A JP10224784A JP10224784A JPS60244294A JP S60244294 A JPS60244294 A JP S60244294A JP 10224784 A JP10224784 A JP 10224784A JP 10224784 A JP10224784 A JP 10224784A JP S60244294 A JPS60244294 A JP S60244294A
- Authority
- JP
- Japan
- Prior art keywords
- alcohol
- fermenter
- fermentation
- cellulose
- cellulosic
- 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.)
- Granted
Links
Landscapes
- Preparation Of Compounds By Using Micro-Organisms (AREA)
Abstract
Description
【発明の詳細な説明】
本発HAはセルロースを基質とし、これから高濃度アル
コールを半連続的に高収率で製造する方法に関する。DETAILED DESCRIPTION OF THE INVENTION The present HA uses cellulose as a substrate and relates to a method for semi-continuously producing high-concentration alcohol at high yields from cellulose.
従来、生物学的手段にょシ、セルロース性物質からアル
コ−kf製造する方法としては、主として次の3つの方
法が知られて釣る。[F]セルロース性動物質セルロー
ス分解酵素を作用させてグルコースを生成させ、次−で
とのグルコースにアルコール生産能を有する微生物(以
下、「アルコール生産微生物」と称する仁ともめる)を
作用させる方法。■セルロース性物質にセルロース分解
酵素とアルコール生産微生物を同時に作用させ、同−発
酵槽中で糖化とアルコール発酵を行う、所謂糖化発酵並
行方式(ssy)による方法。■セルロース性物質にセ
ルロース発酵性細菌を作用させて、一段階でアルコール
を製造する方法。Conventionally, the following three methods are known as methods for producing alcohol from cellulosic materials by biological means. [F] A method in which a cellulosic animal cellulose-degrading enzyme is made to act to produce glucose, and then a microorganism capable of producing alcohol (hereinafter referred to as "alcohol-producing microorganism") is made to act on the glucose. . ■ A method using the so-called parallel saccharification and fermentation method (ssy), in which cellulose-degrading enzymes and alcohol-producing microorganisms are simultaneously applied to cellulosic substances, and saccharification and alcohol fermentation are carried out in the same fermenter. ■A method for producing alcohol in one step by allowing cellulose-fermenting bacteria to act on cellulosic substances.
しかしながら、■の方法は、セルロース分解酵素による
糖化工程金倉まないので、■及び■の方法に比較して工
程が単純でおるが、最終アルコール濃度が低く、!fた
菌の増殖速度が遅いなどの欠点がめシ、未だ実用に供さ
れていない。However, method (2) does not involve the saccharification step using cellulose degrading enzymes, so the process is simpler than methods (2) and (2), but the final alcohol concentration is lower! Due to drawbacks such as the slow growth rate of bacteria, it has not yet been put to practical use.
■の方法は、固定化微生物等を用いた連続発酵が可能で
あるが、セルロース性物質より一グρコース全生成する
反応におりて生産物阻害が生じ、セルロース分解速度及
び最終分解率が劣ることが認められており、高濃度の糖
化’?ll調製することが極めて困難でるるという欠点
を有する。Method (2) allows continuous fermentation using immobilized microorganisms, etc., but product inhibition occurs due to the reaction in which all 1 g ρ course is produced from cellulosic substances, and the cellulose decomposition rate and final decomposition rate are inferior. It is recognized that 'high concentration of glycation'? It has the disadvantage that it is extremely difficult to prepare.
また、■の方法は、糖化とアルコール発酵を同一発酵槽
中で一挙に行うことができるので、反応系が簡略化され
、かつ上々ロース糖化速度、最終糖化率が増大するとい
う利点はおるが、操作上、固定化微生物等音用−る連続
発酵は困難でめり、回分的にアルコール生産微生物を培
養して添加しなければならないという欠点を有する。In addition, method (2) has the advantage that saccharification and alcohol fermentation can be performed all at once in the same fermenter, so the reaction system is simplified and the loin saccharification rate and final saccharification rate are increased. In terms of operation, continuous fermentation using immobilized microorganisms is difficult and difficult, and alcohol-producing microorganisms have to be cultured and added in batches.
斯かる実情において、本発明者は、上記欠点を克服せん
と鋭意研究を行い、セルロース性物質にセルロース分解
#素とアルコール生産微生物全同時に作用させる前記■
の方法において、所定時間間隔毎に発酵醪の一部(V2
〜2/3量)を抜き取シ、残液に抜き取った量に相当す
る基質(セルロース性物質)とセルロース分解酵素全補
給して糖化発酵を繰シ返し穴ところ、発酵醪中のアルコ
ール生産微生物が増殖し、半連続的に比較的高濃度のア
ルコールが製造されることを見出し穴。Under these circumstances, the present inventor conducted intensive research in order to overcome the above-mentioned drawbacks, and in order to overcome the above-mentioned drawbacks, the present inventor conducted the above-mentioned method (1) in which cellulose-degrading elements and alcohol-producing microorganisms are simultaneously applied to cellulosic substances.
In the method, a portion of the fermented mash (V2
~2/3 of the amount) is removed, and the remaining liquid is replenished with the substrate (cellulosic material) corresponding to the amount extracted and all of the cellulolytic enzymes, and the saccharification and fermentation is repeated. Finally, the alcohol-producing microorganisms in the fermented moromi. The holes were found to grow and semi-continuously produce relatively high concentrations of alcohol.
しかし、この方法では、セルロース性物質の濃度を高め
ると反応液の流動性が著しく低、下するため半連続運転
が困難となり、またセルロース性物質がアルコール生産
微生物の増殖を抑えるようになるため補給するセルロー
ス性物質の量が制約を受けることがある。However, with this method, increasing the concentration of cellulosic substances significantly lowers the fluidity of the reaction solution, making semi-continuous operation difficult, and the cellulosic substances suppress the growth of alcohol-producing microorganisms, so replenishment is difficult. The amount of cellulosic material used may be limited.
そこで、本発明者は更に研究を行い、2つの発酵槽を使
用し、その一つ(第1発酵槽)でhセルロース性物質の
糖化とアルコール生産微生物の増殖に適し大条件下で同
時糖化発酵を行い、他の1つ(第2発酵槽)では、第1
発酵槽で得た発酵醪を用して、これにセルロース性物質
のみを添加して糖化発酵を行えば高濃度アルコールが半
連続的に製造されることを見出し、本発明を完成した。Therefore, the present inventor conducted further research and used two fermenters, one of which (the first fermenter) carried out simultaneous saccharification and fermentation under conditions suitable for the saccharification of cellulosic substances and the growth of alcohol-producing microorganisms. In the other one (second fermenter),
The present invention has been completed based on the discovery that high-concentration alcohol can be produced semi-continuously by adding only cellulosic substances to the fermented mash obtained in a fermenter and carrying out saccharification and fermentation.
すなわち、本発明は、第1発酵槽にセルロース性物質、
セルロース分解酵素及びアルコール発酵能含有する微生
物を加えて同時糖化発酵を行い、その発酵醪の一部全第
2発酵槽に移し、第1発酵槽にはセルロース性物質及び
セルロース分解酵素を補給して同時糖化発#を行い、ま
た第2発酵槽にはセルロース性物質のみ會加えて糖化発
酵を行い、第2発酵槽からアルコ−/I/全採取するこ
とを特徴とするセルロースから高濃度アルコ−iI/’
fc半連続的に製造する方法を提供するものでるる。That is, the present invention provides a first fermenter with a cellulosic material,
Simultaneous saccharification and fermentation is performed by adding cellulose-degrading enzymes and microorganisms containing alcoholic fermentation ability, and a portion of the fermented mash is entirely transferred to the second fermenter, and the first fermenter is supplemented with cellulose substances and cellulose-degrading enzymes. Highly concentrated alcohol from cellulose is characterized in that simultaneous saccharification and fermentation are carried out, only cellulosic substances are added to the second fermenter, saccharification and fermentation is carried out, and all alcohol/I/alcohol is collected from the second fermenter. iI/'
This article provides a method for semi-continuously producing fc.
本発明において原料物質として用いられるセル−−ス性
物質としては、純セルロースもしくは木材、稲わら、バ
ガスなどの農林産物、新聞紙、ダンゴール紙などのセル
ロースを主要構成分とする物質が挙げられる。木材、稲
わら、バガスなどの農林産物は粉砕、破砕又はアルカリ
処理等の物理的るるいは化学的前処理を行つkもの全使
用するのが好ましい。Examples of the cellulosic substance used as a raw material in the present invention include pure cellulose, wood, agricultural and forestry products such as rice straw and bagasse, and substances whose main constituent is cellulose such as newspaper and Dangor paper. It is preferable to use all agricultural and forestry products such as wood, rice straw, bagasse, etc. that undergo physical cleaning or chemical pretreatment such as crushing, crushing, or alkali treatment.
また、セルロース分解酵素としては、市販の各種のセル
ラーゼ製剤あるいはトリコデルマ・リーセイなどのセル
ラーゼ生産菌を培養して得られる酵素液が利用できる。Furthermore, as the cellulolytic enzyme, various commercially available cellulase preparations or enzyme solutions obtained by culturing cellulase-producing bacteria such as Trichoderma reesei can be used.
更にまた、アルコール生産微生物としては、8acch
aromyces cerevisiolSaccba
rOmycθeuvarum、8accbaromyc
es forinojensis 6どのアルコール生
産性酵母、めるいはZymOmOnasmoklili
8のようなアルコール生産性細菌などが利用できるが、
セルロースからのアルコ−l生産を効率よく行うには、
耐熱性らるいは好熱油のアルコール生産菌全使用するこ
とが好ましφ。Furthermore, as alcohol-producing microorganisms, 8acch
aromyces cerevisiol Saccba
rOmycθeuvarum, 8accbaromyc
es forinojensis 6 Which alcohol-producing yeast, Merui is ZymOmOnasmoklili
Alcohol-producing bacteria such as No. 8 can be used, but
In order to efficiently produce alcohol from cellulose,
It is preferable to use all heat-resistant oil or thermophilic oil-producing bacteriaφ.
第1発酵槽における反応条件は、セルロース性物質がセ
ルロース分解酵素にニジ速やかに糖化されアルコール生
産微生物が安定して増殖を繰り返す条件が好ましく、使
用するセルロース性物質、セルロース分解酵i、フルコ
ール生産微生物によっても異なるが、温度30〜40℃
、反応時間10〜30時間、発酵醪の最終濃度g V
/ V%以下、特に5〜7V/Vチが好ましい。The reaction conditions in the first fermenter are preferably such that the cellulosic substance is rapidly saccharified by the cellulose-degrading enzyme and the alcohol-producing microorganisms are stably and repeatedly proliferated. Although it varies depending on the temperature, the temperature is 30-40℃
, reaction time 10 to 30 hours, final concentration of fermented mash g V
/V% or less, particularly preferably 5 to 7V/V%.
斯くして発酵を行った後、その発酵醪の一部、好ましく
は172〜2/3を抜き取って第2発酵槽に移される。After fermentation is carried out in this manner, a portion of the fermented mash, preferably 172 to 2/3, is extracted and transferred to a second fermenter.
第1発酵槽の残液には抜き取ったものと略同量のセルロ
ース性物質と更にセルロース分解酵素全補給して発酵を
行う。同第1発酵槽には、酵母エキス、?リペプトンコ
〜ンステイープリカー等の栄養源を添加することもでき
る。The remaining liquid in the first fermenter is supplemented with approximately the same amount of cellulosic material as that which was removed, and all of the cellulose decomposing enzymes are added to carry out fermentation. The first fermenter contains yeast extract, ? Nutrient sources such as lipeptone corn staple liquor can also be added.
第2発酵槽には、第1槽から移行するセルロース分解酵
素及びアルコール生産微生物によって糖化発酵される量
のセルロース性物質を固形のfま加え発酵全行う。この
発酵は、30〜40℃で24〜48時間行うのが好まし
い。このようにすると、第2発酵槽では更に2〜4V/
V%のアルコールが生産され、最終濃度約107/V%
の高濃度アルコールが得られる。In the second fermentation tank, a solid quantity of cellulosic material is added in an amount to be saccharified and fermented by the cellulose-degrading enzyme and alcohol-producing microorganism transferred from the first tank, and the entire fermentation is carried out. This fermentation is preferably carried out at 30-40°C for 24-48 hours. In this way, the second fermenter will have an additional 2 to 4 V/
V% alcohol is produced, with a final concentration of approximately 107/V%
A high concentration of alcohol is obtained.
以上述べたように、本発明によると、セルロース性物質
よ)アルコールを製造するに際し、七ルロース分解酵素
とアルコール生産微生物を同時に作用させ効率的にセル
ロース性物質からのアルコール生産を行し、その上半連
続操作によシ酒母O製造全不要とし、また2つの発酵槽
を使用することによシ、従来の方法に比べ効率的に一層
高黴度のアルコール生産が可能でめるので、本発明はバ
イオマス転換エネルギーとしてのセルロース性物質から
のアルコール生産に有力な工業的方法を提供するもので
るる。As described above, according to the present invention, when producing alcohol (from cellulosic substances), heptalulose-degrading enzyme and alcohol-producing microorganisms act simultaneously to efficiently produce alcohol from cellulosic substances, and then The semi-continuous operation eliminates the need to produce sake mash at all, and the use of two fermenters makes it possible to produce alcohol with a higher mold content more efficiently than conventional methods. provides a promising industrial method for alcohol production from cellulosic materials as biomass conversion energy.
次に実施例を挙けて説明する。Next, an example will be given and explained.
実施例1゜
本実施例では、攪拌機を備え71v2J容の発酵槽を使
用して行った。Example 1 In this example, a 71v2J capacity fermenter equipped with a stirrer was used.
(1ン 第1発酵槽に、市販のトリコデルマ起源のセル
ラーゼ製剤TAP −6(大野製薬(銅製)100Pを
p)l 4.8 、0.05 Mクエン酸緩衝液に溶解
した酵素液IJ、セルロース性物質としてアルカリ処理
バガス(セルロース含量81%)250?、栄養源とし
て酵母エキス3t、麦芽エキス3F、&lJペゾトン5
9.さらに前培養によシ得られた酵母(Saccbar
omyces uvarum ATo(!26602)
全1−当9108個になるように添加し、培養温度37
℃、攪拌数300rpmの栄件で反応を開始した。仕込
み開始から24時間後、発酵醪の2ン3量を第2発酵槽
に送った。第1発酵槽には、抜き取った発酵醪に相当す
るアルカリ処理バガス167f、栄養源およびセルラー
ゼ製剤66fを溶解し大酵素液666m’を添加し、上
記と同様にして発酵全行い、これを繰シ返した。その結
果は第1表に示すとおシでめシ、酵母は安定に増殖を繰
シ返し、約77/V饅のアル・コールが25日間安定に
生産された。(In the first fermenter, add commercially available Trichoderma-derived cellulase preparation TAP-6 (Ohno Pharmaceutical Co., Ltd. (copper) 100P), enzyme solution IJ dissolved in 0.05 M citrate buffer, and cellulose. Alkali-treated bagasse (cellulose content 81%) 250? as a sexual substance, yeast extract 3t, malt extract 3F, &lJ Pezoton 5 as a nutritional source
9. Furthermore, yeast (Saccbar) obtained by pre-culture
omyces uvarum ATo(!26602)
Add so that the total is 9108 pieces, and culture temperature 37
The reaction was started at a temperature of 300 rpm and a stirring speed of 300 rpm. 24 hours after the start of preparation, 2 to 3 amounts of the fermented mash was sent to the second fermenter. To the first fermentation tank, 167f of alkali-treated bagasse corresponding to the extracted fermented mash, 66f of nutrients and cellulase preparations were dissolved, and 666m' of large enzyme solution was added, fermentation was carried out in the same manner as above, and this was repeated. I returned it. The results are shown in Table 1. Oshidemeshi and yeast repeatedly multiplied stably, and approximately 77/V of alcohol was stably produced for 25 days.
(i+) 第2発酵槽の発酵醪にアルカリ処理バガス6
6ft加え、37℃、300 rpmで48時間発#を
行った。その結果は第1表のとおシでめシ、約10V/
V%のアルコールが安定して生産された。(i+) Alkali-treated bagasse 6 is added to the fermented mash in the second fermenter.
6 ft was added, and irradiation was carried out at 37° C. and 300 rpm for 48 hours. The results are as shown in Table 1, approximately 10V/
V% alcohol was stably produced.
第1表
実施例2゜
セルロース分解酵素として、トリコデルマ・リーセイの
セルラーゼ高生産変異株の培養液を濾過して得た酵素液
を使用し、第1発酵槽及び第2発酵槽へのアルカリ処理
バガスの添加量をそれぞれ150F (2回目以後は1
00? )及びsatとし、第2発酵槽の発酵を24時
間とする以外は実施例1と同様に操作した。その結果は
第2表のとお)でめ)、第2発酵槽から77/V56の
アルコールが14日間安定して収得された。Table 1 Example 2 An enzyme solution obtained by filtering the culture solution of a cellulase-producing mutant strain of Trichoderma reesei was used as a cellulose-degrading enzyme, and the alkali-treated bagasse was added to the first and second fermenters. Addition amount of 150F (from second time onwards, 150F
00? ) and sat, and the operation was carried out in the same manner as in Example 1, except that the fermentation in the second fermenter was carried out for 24 hours. The results are shown in Table 2), and alcohol of 77/V56 was stably obtained from the second fermenter for 14 days.
以下余白 第2表 以上Margin below Table 2 that's all
Claims (1)
素及びアルコール発酵能を有する微生物を加えて同時糖
化発酵を行11その発醪醪の一部全第2発酵槽に移し、
第1発酵槽にはセルロース性物質及びセルロース分解酵
素を補給して発酵を行い、また第2発酵槽にはセルロー
ス性物質のみを加えて同時糖化発酵を行い、第、2発酵
槽からアルコ−/I/を採取するこ・と全特徴とするセ
/I/c2−スから高濃度アルコールを半連続的に製造
する方法。L. Cellulosic substances, cellulolytic enzymes, and microorganisms capable of alcoholic fermentation are added to the first fermenter for simultaneous saccharification and fermentation.
The first fermenter is supplemented with cellulosic substances and cellulolytic enzymes for fermentation, and the second fermenter is supplemented with only cellulosic substances for simultaneous saccharification and fermentation. A method for semi-continuously producing high concentration alcohol from a ce/I/c2-se, which is characterized by collecting I/.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10224784A JPS60244294A (en) | 1984-05-21 | 1984-05-21 | Process for semicontinuous production of alcohol in high concentration from cellulose |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10224784A JPS60244294A (en) | 1984-05-21 | 1984-05-21 | Process for semicontinuous production of alcohol in high concentration from cellulose |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS60244294A true JPS60244294A (en) | 1985-12-04 |
JPH0358715B2 JPH0358715B2 (en) | 1991-09-06 |
Family
ID=14322276
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP10224784A Granted JPS60244294A (en) | 1984-05-21 | 1984-05-21 | Process for semicontinuous production of alcohol in high concentration from cellulose |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS60244294A (en) |
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1987006269A1 (en) * | 1986-04-16 | 1987-10-22 | Sumitomo Chemical Company, Limited | Process for preparing optically active cyclopropanecarboxylic acids |
JP2000340238A (en) * | 1999-05-31 | 2000-12-08 | Nippon Shokuryo Kk | Energy supply system of dwelling house or the like using photovoltaic power generation and fuel cell power generation |
WO2008047679A1 (en) * | 2006-10-16 | 2008-04-24 | National Institute Of Advanced Industrial Science And Technology | Ethanol producing process and apparatus |
JP2008092910A (en) * | 2006-10-16 | 2008-04-24 | Forestry & Forest Products Research Institute | Method for producing ethanol |
JP2008253153A (en) * | 2007-03-30 | 2008-10-23 | Mitsui Eng & Shipbuild Co Ltd | Method for producing alcohol |
JP2010536375A (en) * | 2007-08-22 | 2010-12-02 | イー・アイ・デュポン・ドウ・ヌムール・アンド・カンパニー | Method for concentrated biomass saccharification |
JP2011135863A (en) * | 2009-12-04 | 2011-07-14 | Ehime Prefecture | Method for producing microorganism-fermented product |
JP2011139686A (en) * | 2010-01-08 | 2011-07-21 | Oji Paper Co Ltd | Continuous method for producing ethanol by parallel saccharifying fermentation reaction |
-
1984
- 1984-05-21 JP JP10224784A patent/JPS60244294A/en active Granted
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1987006269A1 (en) * | 1986-04-16 | 1987-10-22 | Sumitomo Chemical Company, Limited | Process for preparing optically active cyclopropanecarboxylic acids |
JP2000340238A (en) * | 1999-05-31 | 2000-12-08 | Nippon Shokuryo Kk | Energy supply system of dwelling house or the like using photovoltaic power generation and fuel cell power generation |
WO2008047679A1 (en) * | 2006-10-16 | 2008-04-24 | National Institute Of Advanced Industrial Science And Technology | Ethanol producing process and apparatus |
JP2008092910A (en) * | 2006-10-16 | 2008-04-24 | Forestry & Forest Products Research Institute | Method for producing ethanol |
JP2008253153A (en) * | 2007-03-30 | 2008-10-23 | Mitsui Eng & Shipbuild Co Ltd | Method for producing alcohol |
JP2010536375A (en) * | 2007-08-22 | 2010-12-02 | イー・アイ・デュポン・ドウ・ヌムール・アンド・カンパニー | Method for concentrated biomass saccharification |
JP2011135863A (en) * | 2009-12-04 | 2011-07-14 | Ehime Prefecture | Method for producing microorganism-fermented product |
JP2011139686A (en) * | 2010-01-08 | 2011-07-21 | Oji Paper Co Ltd | Continuous method for producing ethanol by parallel saccharifying fermentation reaction |
Also Published As
Publication number | Publication date |
---|---|
JPH0358715B2 (en) | 1991-09-06 |
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