JPH08291103A - Increase in yield of acetic acid by cellulase - Google Patents
Increase in yield of acetic acid by cellulaseInfo
- Publication number
- JPH08291103A JPH08291103A JP7120742A JP12074295A JPH08291103A JP H08291103 A JPH08291103 A JP H08291103A JP 7120742 A JP7120742 A JP 7120742A JP 12074295 A JP12074295 A JP 12074295A JP H08291103 A JPH08291103 A JP H08291103A
- Authority
- JP
- Japan
- Prior art keywords
- acetic acid
- cellulase
- immobilized
- acid bacteria
- crystalline cellulose
- 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)
- Distillation Of Fermentation Liquor, Processing Of Alcohols, Vinegar And Beer (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、酢酸菌を培養して、酢
酸を製造するセルラーゼによる酢酸増収法に関するもの
である。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for increasing acetic acid yield by cellulase for culturing acetic acid bacteria to produce acetic acid.
【0002】[0002]
【従来の技術】一般に、酢酸菌を用いた酢酸の製造法と
しては、表面醗酵法と全面醗酵法の二つに大別される。2. Description of the Related Art Generally, the method for producing acetic acid using acetic acid bacteria is roughly classified into a surface fermentation method and a full-scale fermentation method.
【0003】このうち、表面醗酵法では、醗酵液の撹拌
と通気は、液表面の菌膜を壊さない程度に緩やかに行わ
れるので、清澄な品質の良い酢酸が得られる利点はある
が、酢酸の濃度はある程度(3〜4%)までしか上がら
ず、また、醸造期間は一カ月から数カ月に亙り、その間
の腐敗の危険性があるという欠点がある。Of these, in the surface fermentation method, since the stirring and aeration of the fermentation solution are carried out gently so as not to destroy the pellicle on the surface of the solution, there is an advantage that acetic acid of clear quality can be obtained. However, the brewing period is from one month to several months, and there is a risk of spoilage during that period.
【0004】これに対し、全面醗酵法では10日前後と
いう短期間で例えば5%程度の高濃度まで上げることは
できるものの、得られる酢酸は、セルロースと菌体から
なる不純物を多く含みやすく、よって濁った品質の悪い
ものとなり、このため清澄な酢酸を得るには吸着剤を加
えた上で濾過を行う必要がある。しかし、全面醗酵法で
得られる酢酸に含まれる不純物としてのセルロースがゲ
ル状膜となり、濾材を詰まらせるので濾過効率は良くな
い。表面醗酵法により得られる酢酸が場合によっては濾
過を必要としない程に清澄な事と対照的であり、又、生
成されたセルロース膜は大量の醗酵液を含み、この醗酵
液が回収されないことによる経済的損失も大きいといえ
る。On the other hand, in the full-scale fermentation method, although it is possible to raise the concentration to a high concentration of, for example, about 5% in a short period of about 10 days, the acetic acid obtained tends to contain a large amount of impurities consisting of cellulose and microbial cells. It becomes turbid and of poor quality, which requires the addition of an adsorbent followed by filtration to obtain clear acetic acid. However, the filtration efficiency is not good because cellulose as an impurity contained in acetic acid obtained by the full-scale fermentation method forms a gel film and clogs the filter medium. This is in contrast to the fact that the acetic acid obtained by the surface fermentation method is so clear as to require no filtration in some cases, and the produced cellulose membrane contains a large amount of fermentation liquid, and this fermentation liquid is not recovered. It can be said that economic loss is also large.
【0005】[0005]
【発明が解決しようとする課題】近年、大規模な工場で
は、大量生産のために全面醗酵法を改良したリアクター
式の製造方法を採用しているが、この方法の場合、セル
ロースの生産能力をもたない菌を培養するために、厳密
な温度管理と周辺環境から隔離された雰囲気を実現して
セルロース生産能力を持った菌の発生を極力抑えること
によって行われていることから、これらの生産管理は非
常に厳密に行われなければならず、小規模の工場では採
用が困難である。In recent years, large-scale factories have adopted a reactor-type production method, which is an improvement of the full-scale fermentation method, for mass production. In the case of this method, the production capacity of cellulose is increased. In order to cultivate non-living bacteria, strict temperature control and an atmosphere that is isolated from the surrounding environment are realized to minimize the generation of bacteria with cellulose production capacity. Management must be very strict and difficult to employ in small factories.
【0006】又、他の酢酸菌の製造法として、例えば特
開昭63−74490号に示されているように、酢酸菌
にセルラーゼを加えて培養する方法も報告されている。As another method for producing acetic acid bacteria, a method of culturing by adding cellulase to acetic acid bacteria has been reported, as disclosed in, for example, JP-A-63-74490.
【0007】この方法は、結晶性セルロースを取るため
に、酢酸菌を高濃度に得る方法を示しているのであっ
て、培養液にエタノールを加えながら培養する酢酸醗酵
ではないし、酢酸濃度の濃い状態でセルラーゼや酢酸菌
を連続的に使用する方法についても十分な検討がなされ
ていない。This method shows a method for obtaining acetic acid bacteria at a high concentration in order to obtain crystalline cellulose. It is not an acetic acid fermentation in which ethanol is added to a culture solution, but a high acetic acid concentration state. The method of continuously using cellulase and acetic acid bacteria has not been sufficiently examined.
【0008】また、ルネ(Rune standal
等)ら(1994年発行、雑誌「J.Bacterio
l」、176巻、665頁)によると、酢酸菌のセルロ
ースの生産に酢酸菌自身の生産する非結晶状態のCMC
(カルボキシメチルセルロース)を分解するセルラーゼ
(CMCアーゼ)が関与するという報告もある。[0008] In addition, Rune standard
Et al. (Published in 1994, magazine “J.Bacterio”)
1 ”, 176, p. 665), the non-crystalline CMC produced by the acetic acid bacterium itself is used for the production of cellulose by the acetic acid bacterium.
There is also a report that cellulase (CMCase) that decomposes (carboxymethyl cellulose) is involved.
【0009】しかしこれらの報告は、山中茂等(199
4年発行、雑誌「化学と生物」、32巻、367頁)の
如く、シート状結晶性の酢酸菌セルロースが力学的強度
に優れ、スピーカー振動板材料に利用される等の高度の
利用があるので、非結晶性セルロースを分解しながら、
結晶性のセルロースを高純度で高収率に取るための一環
であるといえる。However, these reports are reported by Shigeru Yamanaka et al. (199
4th year, magazine "Chemistry and Biology", Vol. 32, p. 367), sheet-like crystalline cellulose acetate has excellent mechanical strength and is highly used as a speaker diaphragm material. So, while decomposing the non-crystalline cellulose,
It can be said that this is a part for obtaining crystalline cellulose with high purity and high yield.
【0010】[0010]
【課題を解決するための手段】本発明は酢酸菌の生産す
る結晶性のセルロースをほぼ完全に分解しながら、清澄
な高品質な酢酸を高収率で得る方法を見い出すことを解
決課題とするもので、第一の発明のセルラーゼによる酢
酸増収法は、酢酸醗酵時にセルラーゼを存在させ、酢酸
菌の生産する結晶性セルロースを分解しながら培養する
ことを特徴とするものである。DISCLOSURE OF THE INVENTION It is an object of the present invention to find a method for obtaining clear, high-quality acetic acid in high yield while almost completely decomposing crystalline cellulose produced by acetic acid bacteria. The method for increasing the amount of acetic acid by cellulase according to the first invention is characterized in that cellulase is present during the fermentation of acetic acid and the crystalline cellulose produced by the acetic acid bacterium is decomposed and cultured.
【0011】又、第二の発明のセルラーゼによる酢酸増
収法は固定化セルラーゼ及び固定化酢酸菌に培養液を接
触させながら培養することを特徴とするものであり、
又、第三の発明のセルラーゼによる酢酸増収法はセルラ
ーゼを陰イオン交換体に吸着させ、多価性反応試薬を反
応させた固定化セルラーゼに酢酸菌を吸着させることを
特徴とするものである。Further, the method for increasing the yield of acetic acid by cellulase of the second invention is characterized by culturing while contacting the culture solution with the immobilized cellulase and the immobilized acetic acid bacterium,
The method for increasing the amount of acetic acid by cellulase of the third invention is characterized by adsorbing cellulase on an anion exchanger and adsorbing acetic acid bacteria on immobilized cellulase reacted with a polyvalent reaction reagent.
【0012】[0012]
【作用】酢酸醗酵時に、セルラーゼを存在させ、酢酸菌
の生産する結晶性セルロースを分解しながら培養すれ
ば、酢酸菌のセルロースは製造されず清澄な酢酸が得ら
れ易くなる他に、セルロース製造に用いられていた糖質
資源が酢酸菌及び酢酸製造に用いられるために、高濃度
培養、高濃度生産が可能となること、及び固定化したセ
ルラーゼ及び固定化した酢酸菌を用いて培養液をその固
定化担体に接触させながら培養すれば、反応の連続化も
可能になる。[Function] When acetic acid is fermented and cellulase is present and cultured while degrading crystalline cellulose produced by acetic acid bacteria, cellulose of acetic acid bacteria is not produced, and clear acetic acid is easily obtained. Since the sugar resource used is used for the production of acetic acid bacteria and acetic acid, high-concentration culture and high-concentration production are possible, and a culture solution is prepared using immobilized cellulase and immobilized acetic acid bacteria. If the culture is carried out while contacting with the immobilized carrier, the reaction can be continued.
【0013】ここに、本発明に用いられる酢酸菌として
は、アセトバクター属あるいはグルコノバクター属に属
する細菌で酢酸醗酵するものであればいずれのものでも
用いられ、又、本発明に用いられるセルラーゼとして
は、結晶性のセルロースを分解する活性を有するセルラ
ーゼであるが、トリコデルマ属のようなセルラーゼ生産
菌の分泌する酵素(CELLULYSINTM、和光純薬
工業株式会社製)等のものであり、又、セルラーゼ製剤
としては、CMCアーゼ、β−グルコシダーゼ等を含む
粗酵素製剤を用いてもよい。As the acetic acid bacterium used in the present invention, any one can be used as long as it can acetic acid-ferment with a bacterium belonging to the genus Acetobacter or Gluconobacter, and the cellulase used in the present invention. As the cellulase having the activity of degrading crystalline cellulose, an enzyme secreted by a cellulase-producing bacterium such as Trichoderma (CELLULYSIN ™ , manufactured by Wako Pure Chemical Industries, Ltd.), etc., As the cellulase preparation, a crude enzyme preparation containing CMCase, β-glucosidase and the like may be used.
【0014】本発明のセルラーゼの反応方法は、酢酸菌
の培養と同時にセルラーゼを作用させ、酢酸菌が結晶性
セルロースを作ったと同時に分解できるようにすること
である。結晶性セルロース生成初期にはセルラーゼが作
用しやすいので、結晶性セルロースの蓄積のない酢酸製
造を実現するには、結晶性セルロース生成初期に作用さ
せることにより、非常に少量のセルラーゼを用いても所
期の目的を実現することが可能となる。The cellulase reaction method of the present invention is to allow cellulase to act at the same time as culturing the acetic acid bacterium so that the acetic acid bacterium can decompose crystalline cellulose at the same time. Since cellulase tends to act in the early stage of crystalline cellulose production, in order to achieve acetic acid production without the accumulation of crystalline cellulose, it is necessary to use it in the early stage of crystalline cellulose production so that even a very small amount of cellulase is used. It is possible to achieve the purpose of the period.
【0015】セルラーゼの存在量は、試験管内で反応し
て、18時間に8.2×10-4%のアビセル(結晶性セ
ルロース)を分解するセルラーゼ量でもほとんど結晶性
セルロースの生成が観察されなかった実施例から推察す
ると、試験管内での反応至適条件で18時間に1×10
-4%以上アビセルを分解するセルラーゼ量で十分であろ
う。As for the existing amount of cellulase, the production of crystalline cellulose was hardly observed even when the amount of cellulase was such that it was reacted in a test tube to decompose 8.2 × 10 -4 % of Avicel (crystalline cellulose) in 18 hours. Inferring from the examples, the reaction in the test tube was optimally 1 × 10 in 18 hours.
An amount of cellulase that decomposes Avicel by -4 % or more will be sufficient.
【0016】ここに比較実験として、試験内において酢
酸菌のセルロース10mg/mlを基質として、結晶性
セルロースを分解する活性の高いセルラーゼ(アビセラ
ーゼ)を高濃度に含むセルラーゼ(0.1%)を用いて
分解した。pH5で50℃、18時間分解しても分解率
が0.05〜0.08%であった。生成されてしまった
力学的強度が強い酢酸菌のセルロースは、強力な結晶性
セルロース分解活性を持つセルラーゼを用いても分解し
にくいことを示している。As a comparative experiment, a cellulase (0.1%) containing a high concentration of cellulase (avicerase) having a high activity of decomposing crystalline cellulose, using 10 mg / ml of cellulose of acetic acid bacteria as a substrate, was used in the test. Was disassembled. The decomposition rate was 0.05 to 0.08% even after decomposition at pH 5 at 50 ° C for 18 hours. It has been shown that the produced cellulose of acetic acid bacterium having a high mechanical strength is difficult to be decomposed even by using cellulase having a strong crystalline cellulose decomposing activity.
【0017】又、可溶性セルラーゼを用いる場合には、
培養濾液を粉末乾燥させた酵素粉末1%程度の酵素溶液
を滅菌フィルターを用いて滅菌したものを培養と同時に
加える方法は容易な方法である。又、酢酸菌の遺伝子上
にアビセラーゼをコードする遺伝子を導入すれば、同様
の効果が得られる。When soluble cellulase is used,
An easy method is to add the enzyme solution of about 1% of enzyme powder obtained by powder-drying the culture filtrate, which is sterilized by using a sterilizing filter, and simultaneously adding it to the culture. In addition, the same effect can be obtained by introducing a gene encoding avicelase onto the gene of acetic acid bacterium.
【0018】ここに、固定化セルラーゼ及び固定化酢酸
菌を用いる場合には、酢酸菌の吸着しやすい滅菌した固
定化セルラーゼを培養と同時に加え、固定化セルラーゼ
に酢酸菌の培養液が絶えず接触するように、振とう、撹
拌、あるいは循環するように培養すると、固定化セルラ
ーゼに酢酸菌の吸着した固定化セルラーゼ及び固定化酢
酸菌が得られる。減菌固定化セルラーゼは、ホルマリ
ン、あるいはエチレンオキサイド等でガス殺菌する方
法、あるいは実施例で示したように、滅菌したセルラー
ゼを、加圧蒸気滅菌した陰イオン交換体に吸着させ、滅
菌した多価性反応試薬を反応させ、滅菌空気を通気しな
がら殺菌灯のもとで乾燥した固定化セルラーゼを用いて
もよい。Here, when the immobilized cellulase and the immobilized acetic acid bacterium are used, a sterilized immobilized cellulase which easily adsorbs the acetic acid bacterium is added at the same time as the culture, and the immobilized cellulase is constantly contacted with the culture solution of the acetic acid bacterium. As described above, by culturing with shaking, stirring, or circulating, the immobilized cellulase and the immobilized acetic acid bacterium in which the immobilized cellulase adsorbs the acetic acid bacterium can be obtained. Sterilized cellulase is a method of gas sterilizing with formalin, ethylene oxide, or the like, or as shown in the examples, sterilized cellulase is adsorbed on an anion exchanger sterilized by pressure steam, and sterilized multivalent. Immobilized cellulase that has been dried under a germicidal lamp while aerating sterile reaction gas with sterilizing air may be used.
【0019】また固定化担体としては、ダイアイオンH
PA−25、WA−21(三菱化成製)、ディオライト
A−4、A−7(住友化学製)、スフェロシルQMA
(ローヌルーラン社製)、バイオサポートCPG500
(エレクトロヌクレオニック社製)、セライト生体触媒
担体R635(マンビル社製)等が用いられる。As the immobilization carrier, diaion H
PA-25, WA-21 (Mitsubishi Kasei), Diolite A-4, A-7 (Sumitomo Chemical), Spherocyl QMA
(Made by Ron-Ne-Roulen), Biosupport CPG500
(Electronucleonic Co., Ltd.), Celite biocatalyst support R635 (Manville Co., Ltd.) and the like are used.
【0020】又、上記担体としては、100オングスト
ローム以上の細孔径を持ち、セルラーゼが結合する面積
の広いポリスチレンやセライトの担体が用いられる。そ
の上、数多くの陰イオン交換基が導入されているので、
酢酸の存在する低pH条件においても、アミノ基等の陽
イオンの静電気的反発力によって、担体表面の微細環境
のプロトン濃度を低くすることが可能である。上述の微
細環境効果のために、酢酸高濃度条件下においても、担
体に結合しているセルラーゼ及び酢酸菌の周辺の環境は
それほど低pHにならず、長時間活性を維持できる利点
を有する担体である。As the above carrier, a carrier of polystyrene or celite having a pore size of 100 angstroms or more and having a wide area for cellulase binding is used. Besides, since many anion exchange groups have been introduced,
Even under a low pH condition in which acetic acid is present, it is possible to lower the proton concentration in the microenvironment on the surface of the carrier by the electrostatic repulsion of cations such as amino groups. Due to the above-mentioned microenvironmental effect, the environment around the cellulase and acetic acid bacteria bound to the carrier does not become so low in pH even under a high concentration of acetic acid, and the carrier has an advantage that the activity can be maintained for a long time. is there.
【0021】また、酢酸菌は上記固定化担体に吸着しや
すいので、固定化セルラーゼに酢酸菌を吸着させること
により固定化酢酸菌が容易に得られ、該固定化セルラー
ゼ及び酢酸菌を用いた連続酢酸醗酵も可能となる。Further, since the acetic acid bacterium is easily adsorbed to the above-mentioned immobilized carrier, the immobilized acetic acid bacterium can be easily obtained by adsorbing the acetic acid bacterium to the immobilized cellulase, and the continuous use of the immobilized cellulase and the acetic acid bacterium. Acetic acid fermentation is also possible.
【0022】その他の、培養条件、培地組成等は、通常
の酢酸醗酵に用いられる公知の方法(1957年発行、
朝井、高井著、雑誌「醗酵工学」35巻、229頁等)
に基づいて培養されるが、高濃度醗酵に関する最近の技
術(1988年発行、森昭彦著、雑誌「微生物」、4
巻、229頁)と併用することも容易である。For other culture conditions, medium composition, etc., known methods used for ordinary acetic acid fermentation (issued in 1957,
Asai and Takai, Magazine "Fermentation Engineering", Vol. 35, p. 229)
The latest technology for high-concentration fermentation (published in 1988, written by Akihiko Mori, magazine "Microorganisms", 4
Vol., P. 229).
【0023】[0023]
【実施例】以下に実施例を示し、本発明を詳しく説明す
る。EXAMPLES The present invention will be described in detail below with reference to examples.
【0024】[実施例1]セルラーゼは、結晶性セルロ
ース分解活性(アビセラーゼ活性)の強いセルラーゼ
(CELLULYSINTM、和光純薬工業株式会社製)
をpH4.5の1/15モルのマックイルベイン緩衝液
に溶解し、1%濃度として培地に加える際に、滅菌フィ
ルター(0.22μmミリポア製)で濾過して無菌化し
た。[Example 1] Cellulase is a cellulase having a strong crystalline cellulose degrading activity (avicellase activity) (CELLULYSIN ™ , manufactured by Wako Pure Chemical Industries, Ltd.).
Was dissolved in 1/15 mol of McIlvain buffer of pH 4.5, and when it was added to the medium as 1% concentration, it was sterilized by filtration with a sterilizing filter (0.22 μm Millipore).
【0025】又、酢酸菌の培養には、酵母エキスを0.
5%、グルコースを3.0%及びポリペプトン2.0%
を含む培地を加圧蒸気滅菌した後、滅菌フィルターで濾
過したエタノールを4.0重量%の濃度になるように無
菌化したエタノールを加え続けた。酢酸菌は、アセトバ
クテリウム キシリナム(理研保存番号JCM7644
でATCC23767)を用いた。前述の培地に粉末寒
天2%を加えて調製した斜面培地とした。使用時には、
前培養として5mlの培地に一植菌耳をとり30℃で一
晩振とうした培養液を1%になるように接種した。For culturing acetic acid bacteria, yeast extract was added to 0.
5%, glucose 3.0% and polypeptone 2.0%
After sterilizing the culture medium containing the above with autoclave, ethanol filtered through a sterilizing filter was sterilized to a concentration of 4.0% by weight, and ethanol was added continuously. Acetobacter is Acetobacterium xylinum (RIKEN preservation number JCM7644
ATCC 23767) was used. A slant medium was prepared by adding 2% of powdered agar to the above medium. When using,
As a preculture, one inoculated ear was taken in 5 ml of medium and shaken overnight at 30 ° C. to inoculate a culture solution at 1%.
【0026】200mlの三角フラスコに、前述の培地
50ml、滅菌したセルラーゼ液5ml、及び前培養し
た種母液0.5mlを加え、30℃で静置培養した。
1、2、3、4、7、10日目にサンプリングを行い、
エタノール濃度を調整した。10日目の培養結果は、表
1のとおりである。なお比較例はセルラーゼを加えない
(5mlの1/15マックイルベイン緩衝液5mlを加
えた)静置培養の結果である。酢酸及びエタノールは、
メタノールを内部標準としてガスクロマトグラフィーで
測定した。菌体重量は、遠心分離して得られた湿重量の
アルカリ加熱処理した際の減少量から求め、結晶性セル
ロースの測定はアルカリ加熱処理後の残留湿重量から求
めた。To a 200 ml Erlenmeyer flask, 50 ml of the above-mentioned medium, 5 ml of sterilized cellulase solution, and 0.5 ml of precultured mother liquor were added, and static culture was carried out at 30 ° C.
Sampling on days 1, 2, 3, 4, 7, 10
The ethanol concentration was adjusted. The results of culture on the 10th day are shown in Table 1. The comparative example is the result of static culture in which cellulase was not added (5 ml of 1/15 McIlbein buffer solution of 5 ml was added). Acetic acid and ethanol are
It was measured by gas chromatography using methanol as an internal standard. The cell weight was obtained from the amount of reduction of the wet weight obtained by centrifugation when the alkali heat treatment was performed, and the measurement of crystalline cellulose was obtained from the residual wet weight after the alkali heat treatment.
【0027】[0027]
【表1】 [Table 1]
【0028】表1から明らかなように、可溶性のセルラ
ーゼをいれて静置培養することにより、結晶性セルロー
スはほとんど生産されず、菌体収量は、123%に増加
し、酢酸収量は、138%に増加した。なお、透過型電
子顕微鏡による観察によると、比較例においては、結晶
状のセルロースが菌体の側面より数多く出ていることが
見られたが、セルラーゼを添加した系では不定形の分泌
物は観察されるが、繊維状の構造物は観察されなかっ
た。As is clear from Table 1, by adding soluble cellulase and statically culturing, almost no crystalline cellulose was produced, the cell yield was increased to 123%, and the acetic acid yield was 138%. Increased. Incidentally, according to the observation with a transmission electron microscope, in the comparative example, it was found that a large amount of crystalline cellulose was emitted from the side surface of the bacterial cell, but in the system to which cellulase was added, an amorphous secretory substance was observed. However, no fibrous structure was observed.
【0029】[実施例2]この実施例においては、振と
う培養した以外は上記実施例1と同様に酢酸菌を培養し
たが、その10日目の培養結果は、表2のごとくであ
る。Example 2 In this example, acetic acid bacteria were cultured in the same manner as in Example 1 except that the culture was carried out with shaking. The results of the 10th day of culture are shown in Table 2.
【0030】[0030]
【表2】 [Table 2]
【0031】表2から明らかなように、可溶性のセルラ
ーゼをいれて振とう培養することにより、結晶性セルロ
ースはほとんど生産されず、菌体収量及び酢酸収量は増
加した。その増加量を表1と比較すると、菌体収量で1
40%、酢酸収量で132%静置培養より振とう培養の
方が高かった。As is clear from Table 2, when the soluble cellulase was added and shake-cultured, crystalline cellulose was hardly produced and the cell yield and acetic acid yield were increased. Comparing the increased amount with Table 1, the cell yield was 1
Shaking culture was higher than static culture at 40% and acetic acid yield of 132%.
【0032】[実施例3]この実施例では、固定化セル
ラーゼは、加圧蒸気殺菌した陰イオン交換体(ダイアイ
オンHPA25三菱化成製)を担体として、実施例1と
同様の1%セルラーゼ溶液を担体1gあたり1ml加え
て18時間振とうしてセルラーゼを担体に吸着させた。
その後、2価性反応試薬グルタールアルデヒドを1/1
5モルのマックイルベイン緩衝液(pH4.5)で2.
5%に調整して滅菌したものを担体1gあたり0.8m
l加え、10分間振とうして反応させた。次に滅菌した
20%亜硫酸水素ナトリウム液を担体1gあたり0.2
ml加えて10分間振とうして、余分なグルタールアル
デヒドを分解した。最後に、滅菌空気を使って吸引濾過
をしながら水洗、濾過及び風乾を殺菌灯のもとで行っ
た。[Example 3] In this example, the immobilized cellulase was prepared by using the same 1% cellulase solution as in Example 1 with an anion exchanger (Diaion HPA25 manufactured by Mitsubishi Kasei) sterilized under pressure steam as a carrier. Cellulase was adsorbed to the carrier by adding 1 ml per 1 g of the carrier and shaking for 18 hours.
Then, divalent reaction reagent glutaraldehyde was added to 1/1
1. With 5 mol of McIlvein buffer (pH 4.5)
0.8m per 1g of carrier after adjusting to 5% and sterilized
1 was added and shaken for 10 minutes to react. Next, sterilized 20% sodium bisulfite solution is added to 0.2 g per 1 g of the carrier.
ml was added and shaken for 10 minutes to decompose excess glutaraldehyde. Finally, washing with water, filtration and air-drying were performed under a germicidal lamp while performing suction filtration using sterile air.
【0033】200mlの三角フラスコに50mlの培
養液を取り、前述した方法で調整した固定化セルラーゼ
を5g及び酢酸菌の種母液0.5mlを加え実施例2と
同様に振とうして培養した。酢酸菌は上記固定化担体に
吸着しやすいので、固定化セルラーゼに酢酸菌が吸着
し、容易に固定化酢酸菌が得られた。固定化したセルラ
ーゼ及び固定化した酢酸菌により10日間培養した結果
は表3のごとくである。50 ml of the culture solution was placed in a 200 ml Erlenmeyer flask, 5 g of the immobilized cellulase prepared by the above-mentioned method and 0.5 ml of the seed liquor of acetic acid bacteria were added, and the mixture was shaken and cultured as in Example 2. Since the acetic acid bacterium was easily adsorbed to the above-mentioned immobilized carrier, the acetic acid bacterium was adsorbed to the immobilized cellulase, and the immobilized acetic acid bacterium was easily obtained. The results of culturing with immobilized cellulase and immobilized acetic acid bacteria for 10 days are shown in Table 3.
【0034】[0034]
【表3】 [Table 3]
【0035】表3から明かなように、固定化セルラーゼ
を用いても結晶性セルロースは、ほとんど生成せず、菌
体量、酢酸生成量は増加した。表2と比べるとその増加
量は少ないが、固定化セルラーゼ及び固定化酢酸菌は繰
り返し使用できるので、その量を増やすことも、連続醗
酵することも容易である。As is clear from Table 3, crystalline cellulose was hardly produced even with the immobilized cellulase, and the cell amount and acetic acid production increased. Although the amount of increase is smaller than that in Table 2, the immobilized cellulase and the immobilized acetic acid bacterium can be repeatedly used, so that the amount can be increased or continuous fermentation can be easily performed.
【0036】[0036]
【発明の効果】本発明は上述の如く、酢酸醗酵に伴う結
晶性のセルロースをほぼ完全に分解し、酢酸の濾過性及
び清澄性の改善に貢献することができ、セルロース生産
に当てられていたエネルギーを酢酸製造に当てるため酢
酸収率を向上することができ、さらに、従来セルロース
膜に含まれているために回収の困難であった醗酵液がセ
ルロース膜がなくなったため、酢酸回収率の向上を図る
ことができる。INDUSTRIAL APPLICABILITY As described above, the present invention is capable of almost completely decomposing crystalline cellulose accompanying acetic acid fermentation, contributing to improvement of filterability and clarification of acetic acid, and was applied to cellulose production. Since the energy can be applied to the production of acetic acid, the yield of acetic acid can be improved. Furthermore, since the fermentation membrane, which was conventionally difficult to collect because it was contained in the cellulose membrane, lost the cellulose membrane, the acetic acid recovery rate was improved. Can be planned.
【0037】また、培養面においては、こんにゃく菌と
も呼ばれ、酢酸醗酵時の有害菌であったアセトバクテリ
ウム キシリナム等の強固なセルロース生産菌の生育条
件下でも全面醗酵法が適用できるのでこんにゃく菌の発
生を防ぐための厳密な生産管理の労力を省き、小規模の
工場でも酢酸の高濃度醗酵を容易なものとすることがで
き、さらに、セルラーゼ及び酢酸菌を、酢酸存在下でも
pH低下の少ない微細環境効果を有す担体に固定化した
ため、高濃度連続醗酵の効率化に大いに貢献するもので
ある。Further, in the culture surface, also called konjac bacterium, since the whole fermentation method can be applied even under the growth conditions of a strong cellulose-producing bacterium such as Acetobacterium xylinum which was a harmful bacterium at the time of acetic acid fermentation, the konjac bacterium can be applied. The labor of strict production control to prevent the generation of lactic acid can be omitted, and high-concentration fermentation of acetic acid can be facilitated even in a small-scale factory.Furthermore, cellulase and acetic acid bacteria can be reduced in pH even in the presence of acetic acid. Since it is immobilized on a carrier with a small microenvironmental effect, it greatly contributes to the efficiency of high-concentration continuous fermentation.
【0038】以上所期の目的を充分達成することができ
る。The above-mentioned intended purpose can be sufficiently achieved.
───────────────────────────────────────────────────── フロントページの続き (72)発明者 笠原 勝次 新潟県見附市学校町2丁目7番13号 新潟 県工業技術センター見附試験場内 ─────────────────────────────────────────────────── ─── Continued Front Page (72) Inventor Katsuji Kasahara 2-7-13 School Town, Mitsuke City, Niigata Prefecture Niigata Prefectural Industrial Technology Center, Mitsuke Proving Ground
Claims (3)
酸菌の生産する結晶性セルロースを分解しながら培養す
ることを特徴とするセルラーゼによる酢酸増収法。1. A method for increasing the yield of acetic acid by cellulase, which comprises culturing while degrading crystalline cellulose produced by an acetic acid bacterium in the presence of cellulase during fermentation of acetic acid.
養液を接触させながら培養することを特徴とする請求項
1記載のセルラーゼによる酢酸増収法。2. The method for increasing the amount of acetic acid by cellulase according to claim 1, wherein the cellulase and the immobilized acetic acid bacterium are cultured while contacting the culture solution.
せ、多価性反応試薬を反応させた固定化セルラーゼに酢
酸菌を吸着させることを特徴とする請求項2記載のセル
ラーゼによる酢酸増収法。3. The method for increasing the amount of acetic acid by cellulase according to claim 2, wherein the cellulase is adsorbed on an anion exchanger, and the acetic acid bacterium is adsorbed on the immobilized cellulase reacted with the polyvalent reaction reagent.
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR20020096432A (en) * | 2001-06-19 | 2002-12-31 | 윤현희 | A Process for Lactic Acid Production |
JP2020000210A (en) * | 2018-07-02 | 2020-01-09 | 株式会社Mizkan Holdings | Fermented cellulose-containing vinegar and manufacturing method therefor |
-
1995
- 1995-04-21 JP JP7120742A patent/JP2717225B2/en not_active Expired - Lifetime
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Title |
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EUR J APPL MICROBIOL BIOTCHNOL=1983 * |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR20020096432A (en) * | 2001-06-19 | 2002-12-31 | 윤현희 | A Process for Lactic Acid Production |
JP2020000210A (en) * | 2018-07-02 | 2020-01-09 | 株式会社Mizkan Holdings | Fermented cellulose-containing vinegar and manufacturing method therefor |
WO2020008984A1 (en) * | 2018-07-02 | 2020-01-09 | 株式会社Mizkan Holdings | Fermented-cellulose-containing vinegar and production method thereof |
CN112292443A (en) * | 2018-07-02 | 2021-01-29 | 味滋康控股有限公司 | Edible vinegar containing fermented cellulose and its preparation method |
EP3819365A4 (en) * | 2018-07-02 | 2022-04-20 | Mizkan Holdings Co., Ltd. | Fermented-cellulose-containing vinegar and production method thereof |
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