JP4854568B2 - Alcohol production method - Google Patents

Alcohol production method Download PDF

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JP4854568B2
JP4854568B2 JP2007095734A JP2007095734A JP4854568B2 JP 4854568 B2 JP4854568 B2 JP 4854568B2 JP 2007095734 A JP2007095734 A JP 2007095734A JP 2007095734 A JP2007095734 A JP 2007095734A JP 4854568 B2 JP4854568 B2 JP 4854568B2
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bacteria
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cells
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正幸 遠山
学 片桐
朋子 岩井
一栄 高岡
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Mitsui Engineering and Shipbuilding Co Ltd
Mitsui E&S Holdings Co Ltd
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    • 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
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Description

本発明はアルコール生産方法に関し、詳しくは菌体酵母をリサイクルするアルコールの連続生産する際に、雑菌に汚染されても、迅速に回復可能なアルコール生産方法に関する。   The present invention relates to an alcohol production method, and more particularly to an alcohol production method that can be quickly recovered even when contaminated with various bacteria during continuous production of alcohol for recycling bacterial yeast.

連続してエタノールを生産する連続エタノール生産方法は、エタノール生産性が高い反面、酵母のエタノール耐性、酸素条件などの環境要因により、エタノール生産効率が大きく変動するため、安定かつ高効率なエタノール生産が困難であった。   The continuous ethanol production method that produces ethanol continuously has high ethanol productivity, but ethanol production efficiency fluctuates greatly depending on environmental factors such as ethanol tolerance of yeast and oxygen conditions, so stable and highly efficient ethanol production is possible. It was difficult.

特に、発酵槽内に連続的にアルコール原料を供給してアルコール発酵を行い、得られたアルコール液を前記発酵槽から引き抜いて、引き抜いたアルコール液中の酵母菌体を沈降分離槽で沈殿させて分離回収して前記発酵槽に返送する菌体リサイクルを行うアルコール連続生産方法は、生産過程が複雑になるため、酵母以外の微生物(雑菌)が混入する可能性が高い。   In particular, the alcohol raw material is continuously fed into the fermenter to perform alcoholic fermentation, the obtained alcohol solution is extracted from the fermenter, and the yeast cells in the extracted alcohol solution are precipitated in a settling tank. The alcohol continuous production method in which the cells are recycled, separated and recovered and returned to the fermenter, has a high possibility of mixing microorganisms other than yeast (miscellaneous bacteria) because the production process becomes complicated.

アルコール生産では、生成物であるエタノールが、生物に対して阻害作用があるため、アルコールに耐性のない微生物が混入しても、アルコール液中では増殖できないので汚染されることは少ない。しかし、通称「火落菌」と呼ばれる乳酸菌に属する一部の菌は、一般に15%のエタノールに対して耐性を持ち増殖が可能であり、中には25%のエタノールでも増殖が可能な、アルコール生産における主要な汚染菌として知られている(非特許文献1)。   In alcohol production, ethanol, which is a product, has an inhibitory effect on living organisms, so even if microorganisms that are not resistant to alcohol are mixed, they cannot be proliferated in an alcoholic solution and are therefore hardly contaminated. However, some bacteria belonging to lactic acid bacteria, commonly called “burning fungi”, are generally resistant to 15% ethanol and can grow, and some can also grow in 25% ethanol. It is known as a major pollutant in (Non-patent Document 1).

従来、雑菌に汚染された場合は、生産を停止し、アルコール液と酵母菌体を全て廃棄して装置を洗浄し、滅菌して再設置し、新たな酵母種菌を接種して立ち上げ直すことが一般的である。元の状態に回復するまで長い期間が必要となれば、それだけ工業的生産量が減少する。
田村學造・野白喜久雄・秋山裕一・小泉武夫編著、「酵母からのチャレンジ〜応用酵母学〜」、技報堂出版、1997年、p.87−90
Conventionally, when contaminated with various bacteria, stop production, discard all alcohol and yeast cells, wash the equipment, sterilize and re-install, inoculate with new yeast inoculum and start up again Is common. If a long period of time is required until the original state is restored, industrial production is reduced accordingly.
Tamura, Kazuo, Nohaku, Kikuo, Akiyama, Yuichi and Koizumi, Takeo, “Challenge from Yeast: Applied Yeastology”, Gihodo Publishing, 1997, p. 87-90

本発明者らは、菌体リサイクルを行うアルコール生産において、雑菌の汚染による損失は、雑菌に汚染された状態から短期間で回復する方法があれば軽減されるのではないかと考え、鋭意研究を継続した結果、本発明に至った。   In the alcohol production in which bacterial cells are recycled, the present inventors consider that the loss due to contamination of various bacteria can be reduced if there is a method for recovering from the state contaminated with various bacteria in a short period of time, and intensive research has been conducted. As a result, the present invention has been reached.

そこで、本発明の課題は、雑菌に汚染された場合、速やかに雑菌を除去し、汚染状態から短期間で回復するアルコールの生産方法を提供することにある。   Accordingly, an object of the present invention is to provide a method for producing alcohol that, when contaminated with various germs, quickly removes the germs and recovers from the contaminated state in a short period of time.

本発明の他の課題は以下の記載によって明らかとなる。   The other subject of this invention becomes clear by the following description.

上記課題は以下の発明によって解決される。   The above problems are solved by the following invention.

(請求項1)
サッカロマイセス属セレビシエ(Saccharomyces cerevisiae)AM12菌株からなる酵母を用いて、発酵槽内に連続的にアルコール原料を供給してアルコール発酵を行い、得られたアルコール液を前記発酵槽から引き抜き、次いで引き抜いたアルコール液中のAM12菌の菌体を沈降分離槽で沈殿させて分離回収して前記発酵槽に返送する菌体リサイクルを行うアルコール生産方法において、
前記沈降分離槽で分離された上澄み液を除去し、沈殿して残ったAM12菌の菌体にエタノール濃度が14%〜20%、pHが6〜8である洗浄液を添加混合し、次いで一定時間静置してAM12菌の菌体を沈殿させ、上澄み液を除去することにより、AM12菌の雑菌汚染を回復することを特徴とするアルコール生産方法。
(Claim 1)
Using yeast consisting of Saccharomyces cerevisiae AM12 strain, the alcohol raw material is continuously fed into the fermenter to perform alcoholic fermentation, and the resulting alcohol solution is withdrawn from the fermenter and then withdrawn alcohol. In the alcohol production method in which the cells of AM12 bacteria in the liquid are precipitated in a sedimentation separation tank, separated and recovered, and returned to the fermentation tank, in which alcohol is recycled.
The supernatant liquid separated in the settling tank is removed, and the washing liquid having an ethanol concentration of 14% to 20% and pH of 6 to 8 is added to and mixed with the AM12 bacteria remaining after precipitation, and then for a certain period of time. A method for producing alcohol, characterized by recovering the contamination of AM12 bacteria by allowing to stand to precipitate the cells of AM12 bacteria and removing the supernatant.

(請求項2)
前記洗浄液を前記AM12菌の菌体に添加混合する際に、前記沈降分離槽から発酵槽へのAM12菌の菌体の返送と、前記発酵槽から沈降分離槽へのアルコール液の送液を停止することを特徴とする請求項1記載のアルコール生産方法。
(Claim 2)
When the washing liquid is added to and mixed with the cells of AM12, the return of the cells of AM12 from the sedimentation tank to the fermentation tank and the feeding of the alcohol liquid from the fermentation tank to the sedimentation tank are stopped. The alcohol production method according to claim 1, wherein:

(請求項3)
前記沈降分離槽内で前記AM12菌の菌体に洗浄液を添加混合した際に、5分以上40分以内静置し、その後上澄み液を沈降分離槽から抜き取ることを特徴とする請求項1又は2記載のアルコール生産方法。
(Claim 3)
3. When the washing liquid is added to and mixed with the cells of AM12 in the sedimentation separation tank, it is allowed to stand for 5 minutes to 40 minutes, and then the supernatant liquid is extracted from the sedimentation separation tank. The alcohol production method as described.

(請求項4)
雑菌を排除する洗浄を、汚染の程度に応じて1または2回以上繰り返すことを特徴とする請求項1〜3の何れかに記載のアルコール生産方法。
(Claim 4)
The alcohol production method according to any one of claims 1 to 3, wherein the washing for eliminating germs is repeated one or more times according to the degree of contamination.

本発明によれば、雑菌に汚染された場合、速やかに雑菌を除去し、汚染状態から短期間で回復するアルコールの生産方法を提供することができる。   ADVANTAGE OF THE INVENTION According to this invention, when contaminated with various germs, the alcohol production method which removes germs rapidly and recovers from a contaminated state in a short period of time can be provided.

以下、本発明の実施の形態を説明する。   Embodiments of the present invention will be described below.

本発明のアルコール生産方法は、凝集沈降性を持つ酵母、好ましくはサッカロマイセス属セレビシエ(Saccharomyces cerevisiae)AM12菌株(以下、AM12菌と称する)からなる酵母を用いて、発酵槽内に連続的にアルコール原料を供給してアルコール発酵を行い、得られたアルコール液を前記発酵槽から引き抜いて、かつ前記引き抜いたアルコール液中の酵母菌体を沈降分離槽で沈殿させて分離回収して前記発酵槽に返送する菌体リサイクルを行うアルコール連続生産方法において、雑菌に汚染された場合に、汚染状態から短期間で回復するための方法である。   The alcohol production method of the present invention uses a yeast having a coagulation sedimentation property, preferably a yeast consisting of Saccharomyces cerevisiae AM12 strain (hereinafter referred to as AM12 strain), continuously in a fermenter. The obtained alcohol solution is extracted from the fermenter, and the yeast cells in the extracted alcohol solution are precipitated and separated and collected in a settling tank, and returned to the fermenter. This is a method for recovering from a contaminated state in a short time when contaminated with various bacteria in a continuous alcohol production method in which cell bodies are recycled.

本発明において、アルコールの生産は、発酵槽に糖液を連続的に供給しながら、一方で生成物を連続的に取り出すもので、エタノールと酵母の混ざった培養液が連続的に取り出されるものを指す。   In the present invention, the alcohol production is to continuously take out the product while continuously supplying the sugar solution to the fermenter, and to continuously take out the culture solution mixed with ethanol and yeast. Point to.

また、本発明における「菌体リサイクルを行う」とは、発酵槽から取り出したエタノールと酵母の混ざった培養液を静置して酵母菌体を沈殿させて分離し、再培養の有無に関わらず分離した菌体の一部を発酵槽に戻してアルコール発酵を行うことと定義される。   In the present invention, “recycling bacterial cells” means that the culture solution mixed with ethanol and yeast taken out from the fermenter is allowed to stand to precipitate and separate the yeast cells, regardless of whether or not re-cultured. It is defined as performing alcoholic fermentation by returning a part of the separated cells to the fermenter.

アルコール生産系は糖液供給タンク、発酵槽、沈降分離槽、それらをつなぐ各ラインを含め、外部から微生物が容易には混入しにくい構造となっている。   The alcohol production system includes a sugar solution supply tank, a fermentation tank, a sedimentation separation tank, and lines connecting them, and has a structure in which microorganisms are not easily mixed from the outside.

本発明において、「雑菌」とは、アルコール生産系に何らかの原因で混入し、存在する酵母以外の微生物のことを指し、「雑菌に汚染される」とは、前記アルコール液中で酵母以外の微生物が増殖し、検出される状態のことであり、「雑菌汚染を回復する」とは、アルコール生産系から酵母以外の微生物を除去し、アルコール連続生産が汚染以前の状態と同様に行われるようにすることである。   In the present invention, “miscellaneous bacteria” refers to microorganisms other than yeast that are mixed in the alcohol production system for some reason, and “contaminated by miscellaneous bacteria” means microorganisms other than yeast in the alcohol solution. Is a state that is proliferated and detected, and “recovering the contamination of germs” means that microorganisms other than yeast are removed from the alcohol production system so that continuous alcohol production is performed in the same manner as before the contamination. It is to be.

本発明に用いられる凝集沈降性酵母AM12菌は工業技術微生物工業技術研究所に、微工研受託番号第6749号として寄託されている。詳しくは特開昭59−135896号公報を参照できる。   The agglutinating sedimentary yeast AM12 used in the present invention has been deposited with the Industrial Technology Microbiology Industrial Technology Research Institute as a fine work laboratory accession number 6749. For details, JP-A-59-135896 can be referred to.

図1に基づいて、本発明のアルコール生産方法を説明する。   The alcohol production method of the present invention will be described based on FIG.

図1において、1は糖液供給タンクであり、2は発酵槽であり、3はアルコール液から菌体を分離する沈降分離槽である。   In FIG. 1, 1 is a sugar liquid supply tank, 2 is a fermenter, and 3 is a sedimentation / separation tank for separating cells from the alcohol liquid.

糖液供給タンク1から発酵槽2への原料の供給は供給ポンプ11、供給ライン12を通して行われる。供給ライン12からは、原料となる糖液のほかペプトンや微量金属塩溶液等の菌体増殖に必要な栄養液も加えることができる。   The raw material is supplied from the sugar solution supply tank 1 to the fermenter 2 through a supply pump 11 and a supply line 12. From the supply line 12, in addition to the sugar solution as a raw material, a nutrient solution necessary for cell growth such as peptone or a trace metal salt solution can be added.

発酵槽2は内部に菌体と供給された原料とを十分に混合するための攪拌装置21を備えている。攪拌装置としては、発酵槽内の混合が十分に行われるものであれば良いが、プロペラ等の攪拌翼を備えたものが好ましく、攪拌回転数は酵母にとって最適値となるように調節される。また、発酵槽には図示しないがpH、温度、溶存酸素濃度を維持するために特に限定されないシステムを備えることができる。   The fermenter 2 includes a stirrer 21 for sufficiently mixing the cells and the supplied raw material. The stirring device may be any device as long as the mixing in the fermenter is sufficiently performed, but a stirring device having a stirring blade such as a propeller is preferable, and the rotation speed of stirring is adjusted to be an optimum value for yeast. Moreover, although not shown in figure, a fermenter can be equipped with the system which is not specifically limited in order to maintain pH, temperature, and dissolved oxygen concentration.

発酵槽2では酵母によってアルコール発酵が行われ、原料糖液はアルコールと酵母菌体を含む液体(培養液)となり、取液ポンプ22、取液ライン23から沈降分離槽3へ送られる。また、アルコール発酵に伴って生じるガスはライン24から排出される。   In the fermenter 2, alcoholic fermentation is performed by yeast, and the raw sugar solution becomes a liquid (culture solution) containing alcohol and yeast cells, and is sent to the sedimentation / separation tank 3 from the collection pump 22 and the collection line 23. In addition, the gas generated along with the alcohol fermentation is discharged from the line 24.

沈降分離槽3では静置による沈降分離が行われ、凝集沈降性酵母は沈降し、アルコール液と分離される。図1において、3aは沈降したAM12菌(酵母)の菌体であり、3bは酵母菌体が除かれた上澄み液であり、通常のアルコール生産が行われている場合にはアルコール液を指す。アルコール液3bはアルコールポンプ31によって引き抜かれ、アルコールライン32を通して次の精製過程へ送られる。   In the sedimentation / separation tank 3, sedimentation / separation is performed by standing, and the coagulating sedimentary yeast settles and is separated from the alcohol liquid. In FIG. 1, 3a is a cell body of precipitated AM12 bacteria (yeast), 3b is a supernatant liquid from which yeast cells have been removed, and refers to an alcohol liquid when normal alcohol production is performed. The alcohol liquid 3b is extracted by the alcohol pump 31 and sent to the next purification process through the alcohol line 32.

沈降し濃縮された菌体3aの一部は取り出され、規定量の菌体がリサイクルポンプ33、供給ライン12へとつながるリサイクルライン34を通して、供給ライン12から原料と共に発酵槽1へ返送される。また、余分な菌体(沈殿物)は排出ライン35より排出される。   A part of the settled and concentrated cells 3a is taken out, and a specified amount of cells are returned to the fermenter 1 from the supply line 12 together with the raw materials through the recycle pump 33 and the recycle line 34 connected to the supply line 12. Further, excess cells (precipitate) are discharged from the discharge line 35.

図1において、4は雑菌に汚染された場合に沈降分離槽3を洗浄する洗浄液を入れる洗浄液タンクであり、41は洗浄液送液ポンプ、42は洗浄液送液ラインである。   In FIG. 1, reference numeral 4 denotes a cleaning liquid tank for containing a cleaning liquid for cleaning the sedimentation / separation tank 3 when contaminated with bacteria, 41 is a cleaning liquid supply pump, and 42 is a cleaning liquid supply line.

図1では、洗浄液送液ライン42は沈降分離槽3の下部に接続されているが、リサイクルライン34に接続し、リサイクルライン34から通常の流路と逆流させるように沈降分離槽3へ洗浄液を注入することもできる。5は、アルコール連続生産系のポンプを制御する制御部である。   In FIG. 1, the cleaning liquid feeding line 42 is connected to the lower part of the sedimentation separation tank 3, but the cleaning liquid is connected to the recycling line 34 and the washing liquid is supplied to the sedimentation separation tank 3 so as to flow backward from the recycling line 34 to the normal flow path. It can also be injected. A control unit 5 controls the alcohol continuous production system pump.

以下に、本発明における雑菌汚染を回復する雑菌の除去方法を説明する。   Below, the removal method of the germ which recovers the germ contamination in this invention is demonstrated.

雑菌による汚染を監視するため、定期的に取液ライン23から沈降分離槽3へ送られた培養液をサンプリングして検査する。   In order to monitor contamination due to various germs, the culture solution sent from the collection line 23 to the sedimentation tank 3 is periodically sampled and inspected.

検査には、迅速な判断が求められることから、培養等による検査法よりは分子生物学的な検査法が好ましく、具体的にはDNAを抽出してPCRを用いて増幅し、増幅後のDNA断片を電気泳動して、例えば、バンドの有無などによって、遺伝子を検出する手法が挙げられ、火落菌など主要な汚染菌に対しては、市販の検査キットを用いることができる。   Since a rapid judgment is required for the test, a molecular biological test method is preferable to a test method such as culture. Specifically, DNA is extracted and amplified using PCR, and the amplified DNA is amplified. For example, a method of detecting a gene by electrophoresis of fragments and detecting the presence or absence of a band can be used, and commercially available test kits can be used for major contaminants such as fire-fung bacteria.

雑菌の検出は、サンプリングしたアルコール液から雑菌の遺伝子を検出するか否かで判定する。   The detection of miscellaneous bacteria is determined by whether or not the gene of miscellaneous bacteria is detected from the sampled alcohol solution.

遺伝子が検出され、雑菌による汚染があると判明した場合、制御部5は供給ポンプ11と、取液ポンプ22とリサイクルポンプ33を停止して、発酵槽への糖液の供給と、発酵槽2から沈降分離槽3の培養液の供給と、沈降分離槽3から発酵槽2への酵母菌体の供給を停止する。   When the gene is detected and it is found that there is contamination by various bacteria, the control unit 5 stops the supply pump 11, the liquid collection pump 22, and the recycle pump 33 to supply the sugar solution to the fermenter and the fermenter 2. The supply of the culture solution in the sedimentation / separation tank 3 and the supply of yeast cells from the sedimentation / separation tank 3 to the fermenter 2 are stopped.

沈降分離槽3内の液体の流入が停止すると、AM12菌は凝集沈降性が高いので速やかに沈降する。混入した微生物は、AM12菌ほど速やかに沈降しないので上澄み液3b中に存在する。この状態にあるとき、制御部5はアルコールポンプ31を稼動させて沈降分離槽3から上澄み液3bを抜き取り、廃棄する。   When the inflow of the liquid in the sedimentation / separation tank 3 stops, the AM12 bacteria settle quickly because of high coagulation sedimentation. Since the contaminated microorganism does not settle as quickly as AM12 bacteria, it exists in the supernatant 3b. In this state, the control unit 5 operates the alcohol pump 31 to extract the supernatant 3b from the sedimentation tank 3 and discard it.

即ち、AM12菌の強い凝集沈降性を利用して、遠心分離機を利用することなく、AM12菌と、沈降速度の異なる雑菌とを分離することができる。   That is, AM12 bacteria can be separated from miscellaneous bacteria having different sedimentation rates without using a centrifuge by utilizing the strong aggregation sedimentation property of AM12 bacteria.

このため、沈降分離槽3への液体の流入(による攪拌)が停止してから、AM12菌を沈降させる時間は5分以上40分以下、好ましくは10分以上30分以下とし、その後、速やかに上澄み液3bを引き抜くことが必要となる。   For this reason, after the inflow of liquid into the sedimentation / separation tank 3 is stopped, the time for sedimentation of AM12 bacteria is 5 minutes to 40 minutes, preferably 10 minutes to 30 minutes, and then promptly. It is necessary to draw out the supernatant 3b.

上澄み液のアルコール培養液をぬきとり廃棄した後、制御部5は洗浄液送液ポンプ41を稼動させ、洗浄液タンク4内の洗浄液を沈降分離槽3下部より注入する。   After wiping off and discarding the alcohol culture solution of the supernatant, the control unit 5 operates the washing solution feed pump 41 to inject the washing solution in the washing solution tank 4 from the lower part of the sedimentation separation tank 3.

洗浄液の組成は、エタノール濃度が14%〜20%、好ましくは14.5%〜17%、pHを6〜8、好ましくは6.5〜7.5に調整し、オートクレーブまたはフィルター等で滅菌をしたものが好ましい。   The composition of the cleaning solution is adjusted to an ethanol concentration of 14% to 20%, preferably 14.5% to 17%, a pH of 6 to 8, preferably 6.5 to 7.5, and sterilized with an autoclave or a filter. Is preferred.

AM12菌は、エタノール濃度20%においても阻害を受けない耐エタノール性を持つが、大抵の他の微生物はエタノール20%の液体中では生存または増殖することができない。   AM12 bacteria have ethanol resistance that is not inhibited even at an ethanol concentration of 20%, but most other microorganisms cannot survive or grow in a 20% ethanol liquid.

火落菌の中でも特に高いエタノール耐性を持つ、Lactobacillus homohiochiiや、L.fructivoransといった真性火落菌といわれる細菌は、本発明の洗浄液の好ましいエタノール濃度では増殖の抑制効果は低いが、これらの菌は生育最適pHが4.5〜5.0であり、pH5.5以上では生育できないので、本発明の、エタノール濃度が14%〜20%、好ましくは14.5%〜17%、pHが6〜8、好ましくは6.5〜7.5である洗浄液は火落菌に対しても効果がある。   Among Lactobacillus, Lactobacillus homohichii, which has particularly high ethanol resistance, Bacteria said to be a true fire bacterium such as Frutivorans have a low growth inhibitory effect at the preferred ethanol concentration of the washing solution of the present invention, but these bacteria have an optimum pH of growth of 4.5 to 5.0, and at pH 5.5 or higher. Since it cannot grow, the cleaning solution of the present invention having an ethanol concentration of 14% to 20%, preferably 14.5% to 17%, pH of 6 to 8, preferably 6.5 to 7.5 is Even if it is effective.

洗浄液ポンプ41は、沈降分離槽3内に沈殿するAM12菌の菌体3aを浮遊させ、沈降分離槽3内でAM12菌の菌体が洗浄液と十分に接触し攪拌することができるような流速で注入可能な出力を持つことが好ましく、1回の洗浄で沈降分離槽容量の50〜80%程度の洗浄液を注入する。沈殿した酵母菌体を浮遊させることで、雑菌の洗浄効果が高くなるためである。   The cleaning liquid pump 41 floats the AM12 bacterial cells 3a that settle in the sedimentation separation tank 3 at a flow rate that allows the AM12 bacterial cells to sufficiently contact and stir the cleaning liquid in the sedimentation separation tank 3. It is preferable to have an injectable output, and a cleaning solution of about 50 to 80% of the sedimentation tank capacity is injected in one cleaning. This is because the effect of washing various bacteria is enhanced by floating the precipitated yeast cells.

洗浄液注入が終了し、攪拌されなくなると速やかにAM12菌は沈降するので、同様に、AM12菌を沈降させる時間は5分以上40分以下、好ましくは10分以上30分以下とし、その後速やかにアルコールポンプ31を稼動させて上澄み液3bを抜き取る。   When the washing liquid injection is completed and the stirring is stopped, the AM12 bacteria quickly settle. Similarly, the AM12 bacteria are allowed to settle for 5 minutes to 40 minutes, preferably 10 minutes to 30 minutes, and then quickly The pump 31 is operated and the supernatant 3b is extracted.

引き抜いた上澄み液3bの洗浄液をサンプリングし、雑菌の遺伝子を検出するか検査する。雑菌の遺伝子が検出されなかった場合は雑菌の除去が完了(雑菌汚染から回復)したとして、通常のアルコール連続生産を開始する。検出した場合は再び洗浄液を注入し、洗浄の工程を雑菌の検出がなくなるまで行う。   A sample of the extracted supernatant 3b is sampled and examined for detection of germ genes. If no germ gene is detected, normal alcohol continuous production is started on the assumption that the removal of the germ has been completed (recovered from contamination). If detected, the washing solution is injected again and the washing process is performed until no bacteria are detected.

以上の洗浄の工程について、制御部5が行う制御処理を図2に示す。   FIG. 2 shows a control process performed by the control unit 5 for the above-described cleaning process.

サンプリングした培養液を検査し、検査データを入力する(S1)。検査データ(例えば、バンドの検出の有無)から、雑菌の混入があるかどうか判断する(S2)。雑菌の混入がないと判断された場合は終了する。   The sampled culture solution is inspected and inspection data is input (S1). It is determined from the inspection data (for example, whether or not a band is detected) whether there is any contamination (S2). If it is determined that there is no contamination, the process ends.

雑菌の混入があると判断された場合、供給ポンプ11と、取液ポンプ22とリサイクルポンプ33を停止して、AM12菌を沈殿させた後、アルコールポンプ31を稼動させて沈降分離槽3から上澄みのアルコール液3bを抜き取る(S3)。   If it is determined that there is contamination, the supply pump 11, the intake pump 22 and the recycle pump 33 are stopped to precipitate AM12 bacteria, and then the alcohol pump 31 is operated to obtain supernatant from the sedimentation separation tank 3. The alcohol liquid 3b is extracted (S3).

アルコール液を抜き取った後、洗浄液送液ポンプ41を稼動させ、洗浄液タンク4内の洗浄液を沈降分離槽3下部より注入し、沈殿するAM12菌の菌体3aを浮遊させる(S4)。   After extracting the alcohol liquid, the cleaning liquid feed pump 41 is operated, the cleaning liquid in the cleaning liquid tank 4 is injected from the lower part of the sedimentation separation tank 3, and the cells 3a of the AM12 bacteria that precipitate are suspended (S4).

AM12菌を沈殿させた後、アルコールポンプ31を稼動させて沈降分離槽3から上澄みの洗浄液3bを抜き取る(S5)。   After the AM12 bacteria are precipitated, the alcohol pump 31 is operated and the supernatant washing liquid 3b is extracted from the sedimentation tank 3 (S5).

洗浄液3bをサンプリングして検査し、検査データを入力する(S6)。検査データ(例えば、バンドの検出の有無)から雑菌が存在するかどうか判断する(S7)。雑菌が存在した場合は、S4に戻る。   The cleaning liquid 3b is sampled and inspected, and inspection data is input (S6). It is determined from the inspection data (for example, whether or not a band is detected) whether or not there are any germs (S7). If miscellaneous bacteria exist, the process returns to S4.

雑菌の存在が認められなかった場合、供給ポンプ11、取液ポンプ22と、リサイクルポンプ33、アルコールポンプ31を順次稼動させて発酵槽への糖液の供給と、通常のアルコール連続生産を再開する(S8)。   When the presence of miscellaneous bacteria is not recognized, supply pump 11, take-up pump 22, recycle pump 33, and alcohol pump 31 are sequentially operated to resume the supply of sugar solution to the fermenter and normal continuous alcohol production. (S8).

本発明の方法では、酵母の菌体をほとんど損失せずに雑菌を除去することができるので、アルコール生産において、雑菌の汚染を排除してから通常の運転までの期間を短くすることができる。   In the method of the present invention, it is possible to remove miscellaneous bacteria with almost no loss of yeast cells. Therefore, in alcohol production, it is possible to shorten the period from elimination of miscellaneous bacteria to normal operation.

以下、本発明を実施例に基づき説明するが、本発明はかかる実施例によって限定されない。   EXAMPLES Hereinafter, although this invention is demonstrated based on an Example, this invention is not limited by this Example.

加熱滅菌処理をした発酵槽に、単糖濃度(グルコース換算)20重量%、コーンスティープリカー0.1重量%を含む培地を入れ、AM12菌の種菌を接種しエタノール発酵を開始した。   A medium containing 20% by weight of monosaccharide (converted to glucose) and 0.1% by weight of corn steep liquor was placed in a heat-sterilized fermenter, inoculated with an inoculum of AM12, and ethanol fermentation was started.

エタノール発酵開始から約40時間後に、発酵槽に糖液を連続的に供給しながら、一方で生成物を連続的に取り出す連続エタノール生産を開始し、最終的に希釈率を0.18h-1とし、発酵槽内の酵母菌体、エタノール、グルコースの各成分の濃度が一定状態(定常状態)となり、連続アルコール生産が立ちあがったことを確認した。 About 40 hours after the start of ethanol fermentation, while continuously supplying the sugar solution to the fermenter, continuous ethanol production was started to continuously take out the product, and the dilution rate was finally set to 0.18 h −1. It was confirmed that the concentration of each component of yeast cells, ethanol, and glucose in the fermenter was in a constant state (steady state), and continuous alcohol production was started.

そのアルコール生産系に、意図的に雑菌に汚染された状態を作り出すため、火落菌(L.homohiochii RIB−9134 理研バイオリソースセンター番号 JCM7524)を発酵槽に混入させ、72時間連続生産を行った。   In order to create a state where the alcohol production system was intentionally contaminated with various germs, fire-fung bacteria (L. homohichi RIB-9134 RIKEN BioResource Center No. JCM7524) were mixed in the fermentor and continuous production was performed for 72 hours.

72時間経過後、発酵槽からアルコール培養液をサンプリングし、遠心分離して菌体を集菌した後DNAを抽出し、Takara PCR火落菌検出キット(タカラバイオ(株))を用いて検査したところ、濃いバンドが確認され、火落菌が検出された。   After 72 hours, the alcohol culture solution was sampled from the fermentor, centrifuged to collect the cells, and then the DNA was extracted and examined using the Takara PCR Fire Detection Kit (Takara Bio Inc.). A dark band was confirmed, and fire eradication bacteria were detected.

この雑菌に汚染された状態のアルコール生産系に対して、本発明を用いて雑菌汚染からの回復を試みた。   With respect to the alcohol production system contaminated with this germ, an attempt was made to recover from the contamination by using the present invention.

雑菌が検出されたので、供給ポンプ11と、取液ポンプ22とリサイクルポンプ33を停止して、30分静置し、AM12菌を沈殿させた。   Since miscellaneous bacteria were detected, the supply pump 11, the intake pump 22 and the recycle pump 33 were stopped and allowed to stand for 30 minutes to precipitate AM12 bacteria.

その後、アルコールポンプ31を稼動させて沈降分離槽3から上澄みのアルコール液3bを速やかに抜き取った。   Thereafter, the alcohol pump 31 was operated, and the supernatant alcohol liquid 3b was quickly extracted from the sedimentation tank 3.

アルコール液を抜き取った後、洗浄液送液ポンプ41を稼動させ、洗浄液タンク4内の洗浄液を沈降分離槽3下部より注入し、沈殿するAM12菌の菌体3aを浮遊させた。   After extracting the alcohol liquid, the cleaning liquid feed pump 41 was operated, and the cleaning liquid in the cleaning liquid tank 4 was injected from the lower part of the settling separation tank 3 to float the AM12 bacterial cells 3a to be precipitated.

洗浄液は、pH7、エタノール濃度15%に調整したものを用いた。   The cleaning solution was adjusted to pH 7 and ethanol concentration 15%.

30分静置してAM12菌を沈殿させた後、アルコールポンプ31を稼動させて沈降分離槽3から上澄みの洗浄液3bを抜き取った。   After allowing to stand for 30 minutes to precipitate AM12 bacteria, the alcohol pump 31 was operated, and the supernatant washing liquid 3b was extracted from the sedimentation tank 3.

洗浄液をサンプリングし、火落菌検査をしたところ、薄いバンドが確認され、火落菌が少量検出された。洗浄によって、検出される火落菌量が少なくなった。   When the cleaning solution was sampled and tested for fire bacteria, a thin band was confirmed and a small amount of fire bacteria was detected. The amount of fire-fung bacteria detected was reduced by washing.

再び洗浄液を注入し、洗浄操作を行った。洗浄液をサンプリングし、火落菌検査をしたところ、バンドは確認されなかった。従って、火落菌を除去することができた。   The cleaning liquid was again injected and cleaning operation was performed. When the cleaning solution was sampled and tested for fire-fung bacteria, no band was confirmed. Therefore, it was possible to remove the fire bacteria.

雑菌の存在が認められなかったので、供給ポンプ11、取液ポンプ22と、リサイクルポンプ33、アルコールポンプ31を順次稼動させて、通常のアルコール連続生産を開始した。   Since the presence of various germs was not recognized, normal supply continuous production was started by sequentially operating the supply pump 11, the liquid collecting pump 22, the recycle pump 33, and the alcohol pump 31.

本発明の連続アルコール生産の概略図Schematic of continuous alcohol production of the present invention 制御部が行う制御処理を示す図The figure which shows the control processing which a control part performs

符号の説明Explanation of symbols

1:糖液供給タンク
11:供給ポンプ
12:供給ライン
2:発酵槽
21:攪拌装置
22:取液ポンプ
23:取液ライン
24:ライン
3:沈降分離槽
3a:AM12菌の菌体
3b:上澄み液(アルコール液、洗浄液)
31:アルコールポンプ
32:アルコールライン
33:リサイクルポンプ
34:リサイクルライン
35:排出ライン
4:洗浄液タンク
41:洗浄液送液ポンプ
42:洗浄液送液ライン
5:制御部
1: Sugar solution supply tank 11: Supply pump 12: Supply line 2: Fermenter 21: Stirrer 22: Extraction pump 23: Extraction line 24: Line 3: Sedimentation separation tank 3a: Cell body of AM12 bacteria 3b: Supernatant Liquid (alcohol liquid, cleaning liquid)
31: Alcohol pump 32: Alcohol line 33: Recycle pump 34: Recycle line 35: Discharge line 4: Cleaning liquid tank 41: Cleaning liquid feeding pump 42: Cleaning liquid feeding line 5: Control unit

Claims (4)

サッカロマイセス属セレビシエ(Saccharomyces cerevisiae)AM12菌株からなる酵母を用いて、発酵槽内に連続的にアルコール原料を供給してアルコール発酵を行い、得られたアルコール液を前記発酵槽から引き抜き、次いで引き抜いたアルコール液中のAM12菌の菌体を沈降分離槽で沈殿させて分離回収して前記発酵槽に返送する菌体リサイクルを行うアルコール生産方法において、
前記沈降分離槽で分離された上澄み液を除去し、沈殿して残ったAM12菌の菌体にエタノール濃度が14%〜20%、pHが6〜8である洗浄液を添加混合し、次いで一定時間静置してAM12菌の菌体を沈殿させ、上澄み液を除去することにより、AM12菌の雑菌汚染を回復することを特徴とするアルコール生産方法。
Using yeast consisting of Saccharomyces cerevisiae AM12 strain, the alcohol raw material is continuously fed into the fermenter to perform alcoholic fermentation, and the resulting alcohol solution is withdrawn from the fermenter and then withdrawn alcohol. In the alcohol production method in which the cells of AM12 bacteria in the liquid are precipitated in a sedimentation separation tank, separated and recovered, and returned to the fermentation tank, in which alcohol is recycled.
The supernatant liquid separated in the settling tank is removed, and the washing liquid having an ethanol concentration of 14% to 20% and pH of 6 to 8 is added to and mixed with the AM12 bacteria remaining after precipitation, and then for a certain period of time. A method for producing alcohol, characterized by recovering the contamination of AM12 bacteria by allowing to stand to precipitate the cells of AM12 bacteria and removing the supernatant.
前記洗浄液を前記AM12菌の菌体に添加混合する際に、前記沈降分離槽から発酵槽へのAM12菌の菌体の返送と、前記発酵槽から沈降分離槽へのアルコール液の送液を停止することを特徴とする請求項1記載のアルコール生産方法。   When the washing liquid is added to and mixed with the cells of AM12, the return of the cells of AM12 from the sedimentation tank to the fermentation tank and the feeding of the alcohol liquid from the fermentation tank to the sedimentation tank are stopped. The alcohol production method according to claim 1, wherein: 前記沈降分離槽内で前記AM12菌の菌体に洗浄液を添加混合した際に、5分以上40分以内静置し、その後上澄み液を沈降分離槽から抜き取ることを特徴とする請求項1又は2記載のアルコール生産方法。   3. When the washing liquid is added to and mixed with the cells of AM12 in the sedimentation separation tank, it is allowed to stand for 5 minutes to 40 minutes, and then the supernatant liquid is extracted from the sedimentation separation tank. The alcohol production method as described. 雑菌を排除する洗浄を、汚染の程度に応じて1または2回以上繰り返すことを特徴とする請求項1〜3の何れかに記載のアルコール生産方法。   The alcohol production method according to any one of claims 1 to 3, wherein the washing for eliminating germs is repeated one or more times according to the degree of contamination.
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