JP2007195406A - Method for producing and fermenting ethanol - Google Patents

Method for producing and fermenting ethanol Download PDF

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JP2007195406A
JP2007195406A JP2006014239A JP2006014239A JP2007195406A JP 2007195406 A JP2007195406 A JP 2007195406A JP 2006014239 A JP2006014239 A JP 2006014239A JP 2006014239 A JP2006014239 A JP 2006014239A JP 2007195406 A JP2007195406 A JP 2007195406A
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ethanol
producing
palm
alcohol
oil
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Fumiaki Ishizaki
文彬 石崎
Takashi Shimazaki
敬士 島崎
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SHINSEIKI HAKKO KENKYUSHO KK
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SHINSEIKI HAKKO KENKYUSHO KK
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Priority to PCT/JP2007/050799 priority patent/WO2007083746A1/en
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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
    • C12P7/065Ethanol, i.e. non-beverage with microorganisms other than yeasts
    • 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
    • C12P19/00Preparation of compounds containing saccharide radicals
    • C12P19/14Preparation of compounds containing saccharide radicals produced by the action of a carbohydrase (EC 3.2.x), e.g. by alpha-amylase, e.g. by cellulase, hemicellulase
    • 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
    • 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
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/10Process efficiency
    • Y02P20/133Renewable energy sources, e.g. sunlight

Abstract

<P>PROBLEM TO BE SOLVED: To provide a method for producing and fermenting ethanol by which the ethanol can efficiently be produced using biomass and a contribution can be made even to a waste liquor treatment causing problems. <P>SOLUTION: The method for producing and fermenting ethanol is carried out as follows. Metroxylon sagu succeeded in artificial cultivation as a plant resource produced in the tropics kept in a wood state is saccharified to remove non-degraded fibers, etc., and POSS (palm oil separator sludge) produced during oil pressing of oil palm widely cultivated in Southeast Asia or a latex mother liquor, etc., obtained from a natural rubber sap are added as an organic nutrient component. An alcohol-producing bacterium Zymomonas mobilis or an alcoholic yeast Saccharomyces cerevisiae is cultivated therein to produce alcohol. Thereby, effects as a method for producing energy from the biomass can be obtained and the contribution can be made to environmental countermeasures in the tropics as a method for treating the waste liquor. <P>COPYRIGHT: (C)2007,JPO&INPIT

Description

地球温暖化と石油資源の枯渇が、同時並行で進む現状に鑑みると、石油の消費を抑制しエネルギー源を光合成産物である再生可能資源に置き換えていくことが人類共通の課題となっている。また、有限資源である石油の先行き不安が高まる中、世界中で自動車用ガソリンにエタノールを添加する動きが拡大しており、ブラジルや米国にとどまらず中国や東南アジア各国でもガソリンへのエタノール添加の動きが拡大しており、燃料エタノール生産のための原料開発や新しい生産法の開発の競争が激化している。   Considering the current situation in which global warming and depletion of petroleum resources proceed in parallel, it is a common challenge for humankind to suppress the consumption of oil and replace energy sources with renewable resources that are photosynthetic products. In addition, as uncertainty about the future of petroleum, which is a limited resource, has increased, movements to add ethanol to gasoline for automobiles are expanding around the world, and not only in Brazil and the United States, but also in countries in China and Southeast Asia The competition for developing raw materials and new production methods for fuel ethanol production is intensifying.

中でも東南アジアの熱帯地方は、光合成能力に富み、バイオマス生産の潜在力が高い上、未開発の植物資源も多い。その中でサゴヤシは現在栽培技術が確立されつつある有望な光合成資源であり、この栽培が実現すればオイルパームに匹敵する大きな光合成エネルギー生産源となり、米国のコーンに並ぶエタノール生産源になるものと思われる。   In particular, the tropical regions of Southeast Asia have a high photosynthesis capacity, high potential for biomass production, and many undeveloped plant resources. Among them, sago palm is a promising photosynthetic resource for which cultivation techniques are currently being established, and if this cultivation is realized, it will become a large source of photosynthetic energy that is comparable to oil palm, and will be an ethanol production source on par with corn in the United States. Seem.

オイルパームは、天然ゴムと並び、代表的な熱帯工業作物である。しかしながら、これらに関する廃液対策技術開発が遅れており、環境対策の点からより合理的な廃液処理技術の開発が望まれている。オイルパーム搾油廃液は嫌気性メタン発酵処理してプランテーションに還元する方法、天然ゴムラテックス母液はラグーン処理を行って無害化する方法などがとられているが、必ずしも十分とは言えない。
特公平6−46941号公報
Oil palm is a typical tropical industrial crop along with natural rubber. However, development of waste liquid countermeasure technology related to these has been delayed, and development of more rational waste liquid treatment technology is desired from the viewpoint of environmental countermeasures. Oil palm extraction waste liquid is treated by anaerobic methane fermentation and reduced to plantation, and natural rubber latex mother liquor is treated by lagoon to make it harmless. However, it is not always sufficient.
Japanese Patent Publication No. 6-46941

さて一般に、微生物の増殖には、アミノ酸やビタミンなどの有機栄養素が必要であるため、アルコール発酵においてデンプン原料を用いる場合、酵母であっても、Zymomonasのような細菌であってもCSLや麦芽エキスのような天然有機栄養源を用いる必要がある。天然ゴムラテックス母液は、豊富な微生物の増殖促進因子を含む魅力ある有機栄養源である(特許文献1)。これは母液を濃縮した上、噴霧乾燥して粉末化したもので、栄養価に富むがコスト的には高価で、エタノール発酵の原料にはなりえない。   Now, since organic nutrients such as amino acids and vitamins are generally required for the growth of microorganisms, when using starch raw materials in alcoholic fermentation, CSL and malt extract can be used for both yeasts and bacteria such as Zymomonas. Natural organic nutrient sources such as Natural rubber latex mother liquor is an attractive organic nutrient source containing abundant microbial growth promoting factors (Patent Document 1). This is a solution obtained by concentrating the mother liquor and spray-drying it into powder, which is rich in nutritional value but expensive in terms of cost and cannot be a raw material for ethanol fermentation.

オイルパーム搾油廃液は、オイルパームの果肉に含まれるタンパク質やビタミン類に富む微生物増殖因子を供給できる安価な有機栄養源と考えられるが、いまだに発酵原料として用いられたことはなく、発明者らが廃液の有効利用の視点からアセトン・ブタノール発酵が可能なことが報告されているにすぎない。   Oil palm extraction waste liquid is considered to be an inexpensive organic nutrient source that can supply microbial growth factors rich in proteins and vitamins contained in the oil palm pulp, but has not yet been used as a fermentation raw material. It has only been reported that acetone / butanol fermentation is possible from the viewpoint of effective use of waste liquid.

そこで本発明は、バイオマスを用いてエタノールを効率よく生産でき、しかも、課題となっている廃液処理にも資することができるエタノール生産発酵法を提供することを目的とする。   Then, this invention aims at providing the ethanol production fermentation method which can produce ethanol efficiently using biomass, and can also contribute to the waste liquid process used as a subject.

第1の発明に係るエタノール生産発酵法は、サゴヤシの原木の粉砕物を用意する第1ステップと、用意した粉砕物に液化酵素及び糖化酵素の少なくとも一方を加え糖化し、糖液を得る第2ステップと、糖液を用いてアルコール生産性細菌及びアルコール酵母の少なくとも一方を培養し、エタノールを生産する第3ステップとを含む。   The ethanol production fermentation method according to the first invention includes a first step of preparing a pulverized product of sago palm, and saccharification by adding at least one of a liquefying enzyme and a saccharifying enzyme to the prepared pulverized product to obtain a sugar solution. And a third step of culturing at least one of alcohol-producing bacteria and alcohol yeast using the sugar solution to produce ethanol.

この構成を採用すれば、後述する実施例から明らかなように、サゴヤシをほぼ原木に近い状態のままで活用し、エタノールを効率よく生産できる。   If this configuration is adopted, as will be apparent from the examples described later, sago palm can be utilized in a state that is almost close to the raw wood, and ethanol can be produced efficiently.

第2の発明に係るエタノール生産発酵法では、第1の発明に加え、第3ステップに先立ち、糖液にオイルパーム搾油廃液を添加する。   In the ethanol production fermentation method according to the second invention, in addition to the first invention, the oil palm extraction waste liquid is added to the sugar solution prior to the third step.

第3の発明に係るエタノール生産発酵法では、第1の発明に加え、第3ステップに先立ち、糖液に天然ゴムラテックス母液を添加する。   In the ethanol production fermentation method according to the third invention, in addition to the first invention, the natural rubber latex mother liquor is added to the sugar solution prior to the third step.

これらの構成により、処理に困難を伴う廃液などを有効活用できる。   With these configurations, waste liquids that are difficult to process can be used effectively.

本発明によれば、バイオマスとしてのサゴヤシから効率よくアルコールを生産できるとともに、廃液を処理するだけでなく有効に活用できる。   ADVANTAGE OF THE INVENTION According to this invention, while being able to produce alcohol efficiently from the sago palm as biomass, not only can a waste liquid be processed but it can be utilized effectively.

サゴヤシは、その原木を粉砕し、繊維質を分別してデンプンを分離し、これを精製・乾燥させてデンプン粉とすれば、コーンスターチ、キャッサバスターチ、ポテトやさつまいもデンプンなどと全く同様デンプン資源として発酵原料になる。しかしながら、サゴヤシを原木のまま発酵原料に供することは、従来技術の常識では不可能と信じられており、未だ誰も検討していない。サゴヤシからデンプンを分離せず、サゴヤシ材木を直接エタノール発酵の原料にすることが可能であれば、サゴヤシからの収率が向上し、プロセスが簡素化するから、大幅なコストダウンが達成でき、画期的な光合成産物からの燃料製法となるに相違ない。   If sago palm is crushed, the fiber is separated, starch is separated, and this is refined and dried to make starch powder. Corn starch, cassava starch, potatoes and sweet potatoes are also a raw material for fermentation as starch resources. become. However, it is believed that the use of sago palm as a raw material for fermentation as raw materials is impossible with conventional common sense, and no one has yet considered it. If starch is not separated from sago palm and sago timber can be directly used as a raw material for ethanol fermentation, the yield from sago palm will be improved and the process will be simplified. It must be a fuel production method from a periodical photosynthesis product.

本発明者らは、これらの知見に基づき、オイルパーム搾油廃液(Palm Oil Separator Sludge=POSS)がエタノール発酵の有機栄養源になりうるかどうか検討した。結晶ブドウ糖培地やサゴデンプン糖化液を炭素源としてPOSSを有機栄養源とし培地添加濃度2−50%の範囲でエタノール細菌Zymomonas mobilisやアルコール酵母Saccharomyces cerevisiaeを培養した。その結果、すべてにおいて菌の増殖は認められないか、増殖してもわずかであった(検討例1参照)。   Based on these findings, the present inventors examined whether oil palm oil extraction waste liquid (Palm Oil Separator Sludge = POSS) can be an organic nutrient source for ethanol fermentation. Ethanol bacteria Zymomonas mobilis and alcohol yeast Saccharomyces cerevisiae were cultured in the range of 2-50% of medium addition concentration using crystalline glucose medium and sago starch saccharified solution as carbon source and POSS as organic nutrient source. As a result, in all cases, the growth of the bacteria was not observed, or even if the growth was slight (see Examination Example 1).

そこで、POSSに含まれる有機物を予め加水分解することによる、有効成分の活性化を試みた。POSSを6N−H2SO4によって110℃、6時間加水分解したもの、Flavourzyme 1000L(Novo)およびAlcalase 2.4LFG(Novo)のプロテアーゼによって酵素分解したものについても発酵試験を行ったが微生物増殖促進活性は発現しなかった。サゴヤシのデンプン糖化液に天然ゴムラテックス母液を有機栄養源としたものでも、アルコール発酵は全くできなかった(検討例2参照)。 Then, activation of the active ingredient was tried by hydrolyzing the organic substance contained in POSS in advance. Fermentation tests were performed on POSS hydrolyzed with 6N—H 2 SO 4 at 110 ° C. for 6 hours, and enzymatically decomposed with Flavorzyme 1000 L (Novo) and Alcalase 2.4 LFG (Novo) protease. No activity was expressed. Alcohol fermentation could not be carried out at all even with a sago starch saccharified solution and a natural rubber latex mother liquor as an organic nutrient source (see Study Example 2).

ところが、驚くべき事に、サゴヤシ原木をそのまま粉砕し、デンプンを分離せずいきなり糖化して得た糖液に、オイルパーム搾油廃液や天然ゴムラテックス母液を適量添加することにより、Zymomonas mobilisに対してもSaccharomyces cerevisiaeにおいても非常に良い発酵性が得られ、ブドウ糖にCSLを用いた標準のエタノール発酵と全く同等の発酵成績を得た。本発明で用いた天然ゴムラテックス母液は、特許文献1と異なり濃縮噴霧乾燥したものでなく、母液そのものであり、コスト的に安価でエタノール発酵の原料として使用可能である。   However, surprisingly, by adding appropriate amounts of oil palm oil extraction waste liquid and natural rubber latex mother liquor to the sugar liquid obtained by pulverizing the raw sago palm as it is, and saccharifying the starch without separating starch, Zymomonas mobilis In Saccharomyces cerevisiae, very good fermentability was obtained, and the fermentation performance was exactly the same as that of standard ethanol fermentation using CSL as glucose. Unlike patent document 1, the natural rubber latex mother liquor used in the present invention is not concentrated spray-dried, but is the mother liquor itself, and can be used as a raw material for ethanol fermentation at low cost.

かくして、本発明者らは、以下述べるとおり、米国のコーンスターチ−CSLの組み合わせを凌駕するバイオマスエタノール生産法を完成した。   Thus, the inventors have completed a biomass ethanol production process that surpasses the US corn starch-CSL combination as described below.

以下、検討例及び実施例を示しながら、本発明を更に詳細に説明する。なお、以下の実施例は、単なる例示であって、本発明はこれらの実施例に限定されないことは言うまでもない。   Hereinafter, the present invention will be described in more detail with reference to examination examples and examples. The following examples are merely illustrative, and it goes without saying that the present invention is not limited to these examples.

(検討例1)
マレーシアSarawak Chemical社製サゴヤシのデンプン100gを秤量し、500ミリリッターの水に縣濁し、pH6.5に調整した後、Termamyl−120L(Novo社)100μリッターを加え90℃で1時間保ち、デンプンの糊化をおこなった。
(Examination example 1)
After weighing 100 g of Sago palm starch produced by Sarawak Chemical Co., Malaysia, suspended in 500 milliliters of water and adjusting to pH 6.5, 100 μl of Termamyl-120L (Novo) was added and kept at 90 ° C. for 1 hour. Gelatinization was performed.

その後pHを4.5とし、Dextrozyme(Novo社)100μリッターを加え70℃に加温し24時間糖化反応を行った結果、ブドウ糖165g/リッターの糖液480ミリリッターを得た。   Thereafter, the pH was adjusted to 4.5, 100 μL of Detrozyme (Novo) was added, and the mixture was heated to 70 ° C. and subjected to a saccharification reaction for 24 hours.

この糖液を水で糖濃度130g/リッターに希釈したもの「5」に対し、マレーシアパームオイル研究所(Malaysia Palm Oil Boad=MPOB)のオイルパーム搾油廃液(Palm Oil Separator Sludge=POSS)「1」を混合し、pH5.8に調整後大型試験管に50ミリリッターを分注し、120℃10分オートクレーブ滅菌した。   This sugar solution is diluted with water to a sugar concentration of 130 g / liter “5”, whereas the oil palm extraction waste fluid (Palm Oil Separator Sludge = POSS) of Malaysia Palm Oil Research Institute (Malaysia Palm Oil Board = MPOB) “1” Were mixed and adjusted to pH 5.8, 50 ml were dispensed into a large test tube, and autoclaved at 120 ° C. for 10 minutes.

これにYMブロス(Difco Laboratories,Detroit)を規定濃度に調整後、試験管に10ミリリッターを分注し115℃で10分間加熱滅菌したもので種培養したZymomonas mobilis NRRL B−14023を1ミリリッター接種し、30℃にて48時間静置発酵した。   To this, YM broth (Difco Laboratories, Detroit) was adjusted to a specified concentration, and 10 ml was dispensed into a test tube and sterilized by heating at 115 ° C. for 10 minutes. Zymomonas mobilis NRRL B-14023 was seed-cultured at 1 ml. Inoculated and left to stand at 30 ° C. for 48 hours.

培養24時間で菌の増殖はわずかに認められたが、エタノールの生成はほとんど認められなかった。培養48時間では菌増殖が認められたものの、培養終了液のエタノール濃度は低くわずかに5g/リッターにとどまっていた。   Slight growth of bacteria was observed in 24 hours of culture, but almost no ethanol was produced. Bacterial growth was observed at 48 hours of culture, but the ethanol concentration of the culture end solution was low and remained at only 5 g / liter.

(検討例2)
検討例1に用いた糖液と同じサゴヤシのデンプン糖化液を用いた。この糖液「1」に対し、インドネシアのNational Timber and Forest Products社の天然ゴムラテックス母液「1」を混合し、pH5.8に調整後大型試験管に50ミリリッターを分注し、120℃10分オートクレーブ滅菌した。
(Examination example 2)
The same sago starch saccharified solution as that used in Study Example 1 was used. Natural sugar latex mother liquor “1” of National Timber and Forest Products of Indonesia is mixed with this sugar liquor “1”, adjusted to pH 5.8, and then dispensed 50 ml into a large test tube. Minute autoclave sterilization.

これにYMブロス(Difco Laboratories,Detroit)を規定濃度に調整後、試験管に10ミリリッターを分注し、115℃で10分間加熱滅菌したもので種培養したZymomonas mobilis NRRL B−14023 1ミリリッターを接種し、30℃にて48時間培養したが菌増殖は認められず、培養液にエタノールは検出されなかった。   To this, YM broth (Difco Laboratories, Detroit) was adjusted to a prescribed concentration, and 10 ml was dispensed into a test tube, which was then sterilized by heating at 115 ° C. for 10 minutes. Zymomonas mobilis NRRL B-14023 1 ml Was inoculated and cultured at 30 ° C. for 48 hours, but no bacterial growth was observed, and ethanol was not detected in the culture solution.

(実施例1)
サゴヤシは、インドネシアのNational Timber and Forest Products社から入手した。これは、サゴヤシ原木を約1−2cm2厚さ3−4mmにしてオーブンで熱風乾燥し、水分約50%としたものである。
Example 1
Sago palm was obtained from National Timber and Forest Products, Indonesia. This is a sago palm log having a thickness of about 1-2 cm 2 and a thickness of 3-4 mm, and hot-air drying in an oven to a moisture content of about 50%.

これを250グラム秤量し乳鉢棒で粉砕後、すり鉢でさらに粉砕し、水900ミリリッターを加えて0.1N−NaOHにてpH6.5に調整し、Termamyl−120L(Novo社)100μリッターを加え90℃に加温し1時間保った。   250 g of this was weighed and pulverized with a mortar stick, then further pulverized with a mortar, 900 ml of water was added, pH was adjusted to 6.5 with 0.1 N NaOH, and Termamyl-120L (Novo) 100 μl was added. Warm to 90 ° C. and hold for 1 hour.

ついでマグネットスターラーで攪拌しながら0.1N−HClにてpHを4.5に調整してDextrozyme(Novo社)100μリッターを加え70℃に加温し、24時間糖化反応を行った。   Subsequently, while stirring with a magnetic stirrer, the pH was adjusted to 4.5 with 0.1 N HCl, dextrozyme (Novo) 100 μL was added, the mixture was heated to 70 ° C., and saccharification reaction was performed for 24 hours.

反応開始後8時間で加水分解率95%に達し、以後分解率はほとんど変化しなかった。糖化した液は1050ミリリッター、糖濃度は160g/リッターであった。   In 8 hours after the start of the reaction, the hydrolysis rate reached 95%, and thereafter the degradation rate hardly changed. The saccharified liquid was 1050 milliliters, and the sugar concentration was 160 g / liter.

この糖液を3,000g 2分遠心分離して固形分を分離した。この糖液を水で糖濃度130g/リッターに希釈したもの「5」に対し、マレーシアパームオイル研究所(Malaysia Palm Oil Boad=MPOB)のオイルパーム搾油廃液(Palm Oil Separator Sludge=POSS)「1」を混合し、pH5.8に調整後大型試験管に50ミリリッターを分注し、120℃10分オートクレーブ滅菌した。   The sugar solution was centrifuged at 3,000 g for 2 minutes to separate the solid content. This sugar solution is diluted with water to a sugar concentration of 130 g / liter “5”, whereas the oil palm extraction waste fluid (Palm Oil Separator Sludge = POSS) of Malaysia Palm Oil Research Institute (Malaysia Palm Oil Board = MPOB) “1” Were mixed and adjusted to pH 5.8, 50 ml were dispensed into a large test tube, and autoclaved at 120 ° C. for 10 minutes.

これにYMブロス(Difco Laboratories, Detroit)を規定濃度に調整後、試験管に10ミリリッターを分注し、115℃で10分間加熱滅菌したもので種培養したZymomonas mobilis NRRL B−14023 1ミリリッターを接種し、30℃にて15時間静置発酵した。   To this, YM broth (Difco Laboratories, Detroit) was adjusted to a specified concentration, and 10 ml was dispensed into a test tube, which was then sterilized by heating at 115 ° C. for 10 minutes. Zymomonas mobilis NRRL B-14023 1 ml And incubating at 15 ° C. for 15 hours.

培養終了液のエタノールをガスクロマトグラフィーで分析し、エタノール濃度63g/リッターを得た。   The ethanol at the end of the culture was analyzed by gas chromatography to obtain an ethanol concentration of 63 g / liter.

(実施例2)
実施例1に用いた糖液と同じサゴヤシ原木糖化液を用いた。
(Example 2)
The same sago palm tree saccharified solution as that used in Example 1 was used.

この糖液「1」に対し、インドネシアのNational Timber and Forest Products社の天然ゴムラテックス母液「1」を混合し、pH5.8に調整後大型試験管に50ミリリッターを分注し、120℃10分オートクレーブ滅菌した。   Natural sugar latex mother liquor “1” of National Timber and Forest Products of Indonesia is mixed with this sugar liquor “1”, adjusted to pH 5.8, and then dispensed 50 ml into a large test tube. Minute autoclave sterilization.

これにYMブロス(Difco Laboratories,Detroit)を規定濃度に調整後、試験管に10ミリリッターを分注し、115℃で10分間加熱滅菌したもので種培養したZymomonas mobilis NRRL B−14023 1ミリリッターを接種し、30℃にて15時間静置発酵した。   To this, YM broth (Difco Laboratories, Detroit) was adjusted to a prescribed concentration, and 10 ml was dispensed into a test tube, which was then sterilized by heating at 115 ° C. for 10 minutes. Zymomonas mobilis NRRL B-14023 1 ml And incubating at 15 ° C. for 15 hours.

培養終了液のエタノールをガスクロマトグラフィーで分析し、エタノール濃度41g/リッターを得た。   The ethanol at the end of the culture was analyzed by gas chromatography to obtain an ethanol concentration of 41 g / liter.

(実施例3)
実施例1に用いた糖液と同じサゴヤシ原木糖化液を用いた。
(Example 3)
The same sago palm tree saccharified solution as that used in Example 1 was used.

この糖液を水で糖濃度130g/リッターに希釈したもの「5」に対し、マレーシアパームオイル研究所(Malaysia Palm Oil Boad=MPOB)のオイルパーム搾油廃液(Palm Oil Separator Sludge=POSS)「1」を混合し、pH5.8に調整後大型試験管に50ミリリッターを分注し、120℃10分オートクレーブ滅菌した。   This sugar solution is diluted with water to a sugar concentration of 130 g / liter “5”, whereas the oil palm extraction waste fluid (Palm Oil Separator Sludge = POSS) of Malaysia Palm Oil Research Institute (Malaysia Palm Oil Board = MPOB) “1” Were mixed and adjusted to pH 5.8, 50 ml were dispensed into a large test tube, and autoclaved at 120 ° C. for 10 minutes.

これにYMブロス(Difco Laboratories,Detroit)を規定濃度に調整後、試験管に10 ミリリッターを分注し115℃で10分間加熱滅菌したもので種培養したアルコール酵母Saccharomyces cerevisiaeを接種し、31.5℃にて24時間静置発酵した。   To this, YM broth (Difco Laboratories, Detroit) was adjusted to a prescribed concentration, 10 ml was dispensed into a test tube, and heat-sterilized at 115 ° C. for 10 minutes, and then inoculated with alcoholic yeast Saccharomyces cerevisiae. The fermentation was performed at 5 ° C. for 24 hours.

培養終了液のエタノールをガスクロマトグラフィーで分析し、エタノール濃度58g/リッターを得た。   The ethanol at the end of the culture was analyzed by gas chromatography to obtain an ethanol concentration of 58 g / liter.

(実施例4)
実施例1で用いたものと同じインドネシアのNational Timber and Forest Products社から入手したサゴヤシチップを用いた。これを200グラム秤量し、乳鉢棒で粉砕後すり鉢でさらに粉砕して水.1.3リッターに縣濁し、0.1N−NaOHにてpH6.5に調整し、Termamyl−120L(Novo社)100μリッターを加え、90℃に加温し1時間保った。
Example 4
The same sago palm chips obtained from National Timber and Forest Products of Indonesia as used in Example 1 were used. This was weighed 200 grams, ground with a mortar and further ground with a mortar. The mixture was suspended in 1.3 liters, adjusted to pH 6.5 with 0.1 N NaOH, Termamyl-120L (Novo) 100 μL was added, heated to 90 ° C. and kept for 1 hour.

ついでガラス棒で攪拌しながら、0.1N−HClにてpHを4.5に調整し、Dextrozyme(Novo社)100μリッターを加え、70℃に加温し24時間糖化反応を行い糖濃度140g/リッターの糖液1.35リッターを得た。
ミリリッターこの糖液を3,000g 2分遠心分離して固形分を分離した後、糖濃度120g/リッターに希釈した。
Next, while stirring with a glass rod, the pH is adjusted to 4.5 with 0.1 N HCl, Dextrozyme (Novo) 100 μL is added, heated to 70 ° C. and subjected to a saccharification reaction for 24 hours to a sugar concentration of 140 g / A 1.35 liter sugar solution of liter was obtained.
Milliliter This sugar solution was centrifuged at 3,000 g for 2 minutes to separate the solid content, and then diluted to a sugar concentration of 120 g / liter.

これに予め9,000g 3分の遠心分離によって固形分(SS)を取り除いたNational Timber and Forest Products社のオイルパーム搾油廃液(POSS)400 ミリリッターを加え、pH5.8に調整後、120℃10分オートクレーブ滅菌した後2リッターガラスジャーに仕込んだ。   To this was added 400 milliliters of oil palm oil expelled waste liquid (POSS) from National Timber and Forest Products, which had previously been freed of solids (SS) by centrifugation at 9,000 g for 3 minutes, adjusted to pH 5.8, and then adjusted to 120 ° C. 10 After autoclaving, the mixture was charged into a 2-liter glass jar.

これにYMブロス(Difco Laboratories,Detroit)を規定濃度に調整後、100ミリリッター Erlenmyer Flaskに入れ、115℃で10分間加熱滅菌した培地で種培養したZymomonas mobilis NRRL B−14023 50ミリリッターを接種し、150rpm、pH5.5、30℃にてエタノール発酵した。   YM broth (Difco Laboratories, Detroit) was adjusted to a prescribed concentration, and then inoculated with Zymomonas mobilis NRRL B-14023 50 milliliter which was put into 100 milliliter Erlenmyer Flask and seeded in a medium sterilized by heating at 115 ° C. for 10 minutes. And ethanol fermentation at 150 rpm, pH 5.5 and 30 ° C.

図1は、アルコール発酵経過(POSS20%)を示し、横軸は時間「CT」である。図1において、「RS」とあるのは、残糖濃度であり、「DCW」は乾燥菌体重量、「EtOH」はエタノール濃度をそれぞれ示す。培養14時間でエタノール47g/リッター(6vol%)、残糖濃度は0であった。   FIG. 1 shows the course of alcoholic fermentation (POSS 20%), and the horizontal axis is time “CT”. In FIG. 1, “RS” indicates the residual sugar concentration, “DCW” indicates the dry cell weight, and “EtOH” indicates the ethanol concentration. After 14 hours of culture, ethanol was 47 g / liter (6 vol%) and the residual sugar concentration was 0.

本発明によるエタノール発酵経過を示すグラフThe graph which shows the ethanol fermentation progress by this invention

Claims (5)

サゴヤシの原木の粉砕物を用意する第1ステップと、
用意した粉砕物に液化酵素及び糖化酵素の少なくとも一方を加え糖化し、糖液を得る第2ステップと、
前記糖液を用いてアルコール生産性細菌及びアルコール酵母の少なくとも一方を培養し、エタノールを生産する第3ステップとを含む、ことを特徴とするエタノール生産発酵法。
A first step of preparing a sago palm crushed material,
A second step of adding at least one of a liquefying enzyme and a saccharifying enzyme to the prepared pulverized product to saccharify and obtain a sugar solution;
And a third step of culturing at least one of alcohol-producing bacteria and alcohol yeast using the sugar solution to produce ethanol.
前記第3ステップに先立ち、前記糖液にオイルパーム搾油廃液を添加する、請求項1記載のエタノール生産発酵法。 The ethanol production fermentation method according to claim 1, wherein an oil palm extraction waste liquid is added to the sugar liquid prior to the third step. 前記第3ステップに先立ち、前記糖液に天然ゴムラテックス母液を添加する、請求項1記載のエタノール生産発酵法。 The ethanol production fermentation method according to claim 1, wherein a natural rubber latex mother liquor is added to the sugar solution prior to the third step. 前記アルコール生産性細菌は、Zymomonas mobilisである、請求項1から3のいずれか記載のエタノール生産発酵法。 The ethanol-producing fermentation method according to any one of claims 1 to 3, wherein the alcohol-producing bacterium is Zymomonas mobilis. 前記アルコール酵母は、Saccharomyces cerevisiaeである、請求項1から4のいずれか記載のエタノール生産発酵法。 The ethanol-producing fermentation method according to any one of claims 1 to 4, wherein the alcoholic yeast is Saccharomyces cerevisiae.
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JP2010099580A (en) * 2008-10-23 2010-05-06 Mitsui Eng & Shipbuild Co Ltd Pretreatment method for use in saccharification of empty fruit bunch, and method of producing ethanol using pretreatment method
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