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JPS6319150B2 - - Google Patents
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JPS6319150B2 - - Google Patents

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Publication number
JPS6319150B2
JPS6319150B2 JP6392780A JP6392780A JPS6319150B2 JP S6319150 B2 JPS6319150 B2 JP S6319150B2 JP 6392780 A JP6392780 A JP 6392780A JP 6392780 A JP6392780 A JP 6392780A JP S6319150 B2 JPS6319150 B2 JP S6319150B2
Authority
JP
Japan
Prior art keywords
cellulose
ozone
degrading bacteria
amount
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.)
Expired
Application number
JP6392780A
Other languages
Japanese (ja)
Other versions
JPS56160989A (en
Inventor
Hitoshi Ishibashi
Masahiko Ishida
Yoji Otahara
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Hitachi Ltd
Original Assignee
Hitachi Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Hitachi Ltd filed Critical Hitachi Ltd
Priority to JP6392780A priority Critical patent/JPS56160989A/en
Publication of JPS56160989A publication Critical patent/JPS56160989A/en
Publication of JPS6319150B2 publication Critical patent/JPS6319150B2/ja
Granted legal-status Critical Current

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  • Enzymes And Modification Thereof (AREA)
  • Micro-Organisms Or Cultivation Processes Thereof (AREA)

Description

【発明の詳现な説明】 本発明は、皲わら、麊わら、バガス、故玙およ
び朚くずなどのセルロヌス性物質を炭玠源ずしお
セルロヌス分解菌の培逊にあたり、セルロヌス分
解菌がセルロヌス性物質のセルロヌスを効率的に
資化できるようにするセルロヌス分解菌培逊方法
に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention provides a method for culturing cellulose-degrading bacteria using cellulosic materials such as rice straw, wheat straw, bagasse, waste paper, and wood chips as a carbon source. This invention relates to a method for culturing cellulose-degrading bacteria to enable cellulose assimilation.

セルロヌス性物質にセルロヌス分解菌を䜜甚さ
せ、セルロヌス分解菌の分泌するセルラヌれセ
ルロヌス加氎分解酵玠や有機酞など、あるいは
セルロヌス分解菌そのものを増殖せしめ埮生物蛋
癜を生産する堎合にセルロヌス分解菌の培逊が必
芁であり、しかもセルロヌス分解菌がセルロヌス
性物質䞭のセルロヌスを効率的に資化できるよう
にせねばならない。しかしながら、皲わら、麊わ
ら、バガス、故玙及び朚くずなどのセルロヌス性
物質䞭のセルロヌスは、セルロヌス分解菌が䜜甚
しにくい化孊構造にな぀おいる。セルロヌスは、
グルコヌスがβ――結合で盎線状に䞊んだ
ホモポリマヌであるが、䞊蚘物質䞭のセルロヌス
は、線状ホモポリマヌ同志が互いに平行に配䜍し
た構造、すなわち結晶構造をずり、しかも、難分
解性のリグニンで芆われおいる。ずころで、セル
ロヌス分解菌がセルロヌスを栄逊源ずしお利甚で
きるのは、同菌が分泌するセルラヌれセルロヌ
ス加氎分解酵玠の䜜甚による。セルラヌれは、
結晶性セルロヌスを非結晶化するC1酵玠、非結
晶性セルロヌスをセロビオヌスに分解するCx酵
玠及びセロビオヌスをグルコヌスに分解するβ―
グルコシダヌれから構成される耇合酵玠である。
セルロヌス分解菌は、このセルラヌれの䜜甚によ
りセルロヌスをセロビオヌスやグルコヌスに䜎分
子化し利甚する。しかしながら、セラヌれはC1
掻性が匱くしかもリグニン分解胜がない。したが
぀お、セルロヌス分解菌は、前述のような構造を
も぀セルロヌス性物質䞭のセルロヌスをそのたた
では資化できない。そのため、セルロヌス性物質
を基質ずしおセルロヌス分解菌を培逊するには、
基質調補時にリグニンの分解やセルロヌスの結晶
構造の砎壊を行う必芁がある。その方法ずしおは
化孊的あるいは物理的な凊理が行われおいる。化
孊的な方法ずしおは、氎酞化ナトリりムなどによ
るアルカリ凊理及びリン酞などによる酞凊理など
があるが、氎酞化ナトリりム氎溶液内にセルロヌ
ス性物質を加えお加熱する方法が䞀般的である。
これは、リグニンを抜出陀去するず共にセルロヌ
スの結晶構造を膚最させる䜜甚をも぀おいる。し
かしながら、この方法は倧量の氎を消費し、しか
もセルロヌス、ヘミセルロヌス及び蛋癜質などの
有効成分の損倱がある。たた難分解性のリグニン
などを含む廃液の凊理が必芁である。䞀方、物理
的凊理ずしおは、ボヌルミルや振動ミルなどに粉
砕が䞀般的である。この方法は、セルロヌス性物
質を400メツシナ皋床に砎砕し、盎接セルロヌス
の結晶構造を砎壊するものである。しかし、この
方法は、セルロヌス性物質を十分に也燥する必芁
があるこず及び動力費が著しく倧きいこずなどの
欠点がある。
When cellulose-degrading bacteria are allowed to act on cellulosic substances and the cellulase (cellulose hydrolase) and organic acids secreted by the cellulose-degrading bacteria are grown, or the cellulose-degrading bacteria themselves are grown to produce microbial proteins, the culture of cellulose-degrading bacteria is used. In addition, it must be possible for cellulose-degrading bacteria to efficiently utilize cellulose in cellulosic substances. However, cellulose in cellulosic materials such as rice straw, wheat straw, bagasse, waste paper, and wood chips has a chemical structure that makes it difficult for cellulose-degrading bacteria to act on it. Cellulose is
It is a homopolymer in which glucose is linearly arranged with β-1,-4 bonds, but the cellulose in the above substance has a structure in which the linear homopolymers are coordinated in parallel to each other, that is, a crystal structure, and furthermore, It is covered with persistent lignin. By the way, the ability of cellulose-degrading bacteria to use cellulose as a nutrient source is due to the action of cellulase (cellulose hydrolase) secreted by the same bacteria. Cellulase is
C1 enzyme that amorphizes crystalline cellulose, Cx enzyme that decomposes amorphous cellulose into cellobiose, and β- enzyme that decomposes cellobiose into glucose.
It is a complex enzyme composed of glucosidase.
Cellulose-degrading bacteria convert cellulose into cellobiose and glucose using the cellulase. However, Cerase is C 1
It has weak activity and no lignin decomposition ability. Therefore, cellulose-degrading bacteria cannot directly assimilate cellulose contained in cellulosic substances having the above-mentioned structure. Therefore, in order to cultivate cellulose-degrading bacteria using cellulosic materials as a substrate,
When preparing the substrate, it is necessary to decompose lignin and destroy the crystal structure of cellulose. Chemical or physical treatment is used as a method for this purpose. Chemical methods include alkaline treatment with sodium hydroxide or the like and acid treatment with phosphoric acid, etc., but a common method is to add a cellulosic substance to an aqueous sodium hydroxide solution and heat it.
This has the effect of extracting and removing lignin and swelling the crystal structure of cellulose. However, this method consumes large amounts of water and there is a loss of active ingredients such as cellulose, hemicellulose and protein. Additionally, it is necessary to treat wastewater containing persistent lignin. On the other hand, as a physical treatment, pulverization using a ball mill, vibration mill, etc. is common. This method crushes cellulosic materials into approximately 400 meshes and directly destroys the crystalline structure of cellulose. However, this method has disadvantages, such as the need to thoroughly dry the cellulosic material and the significant power costs.

本発明の目的は、セルロヌス分解菌をセルロヌ
スを炭玠源ずしお培逊するにあたり、䞊蚘埓来法
の欠点を解消し、セルロヌス分解菌がセルロヌス
性物質䞭のセルロヌスを効率良く利甚できるセル
ロヌス分解菌培逊法を提䟛するものである。
An object of the present invention is to provide a method for culturing cellulose-degrading bacteria that eliminates the drawbacks of the conventional methods described above and allows cellulose-degrading bacteria to efficiently utilize cellulose in cellulose materials. It is something to do.

本発明に぀いお抂説すれば、本発明のセルロヌ
ス分解菌培逊方法は、セルロヌス性物質の含氎率
が90以䞋になるように無機窒玠や無機塩などを
含む氎溶液ず混合し、次いでオゟンず気―固接觊
させるこずにより、セルロヌス分解菌のセルロヌ
ス性物質䞭のセルロヌス資化性を向䞊させるもの
である。
To summarize the present invention, the method for culturing cellulose-degrading bacteria of the present invention involves mixing a cellulosic material with an aqueous solution containing inorganic nitrogen, inorganic salts, etc. so that the water content becomes 90% or less, and then adding ozone and gas-solidified material. By contacting it, the ability of cellulose-degrading bacteria to assimilate cellulose in cellulose substances is improved.

補玙工業の朚材のパルプ化工皋から排出される
リグニン廃液をオゟン凊理するこずによりリグニ
ンが分解するこずが報告されおいる昭和50幎床
文郚省特定研究、暋口隆昌、“オゟン及び埮生物
凊理による廃液リグニンの分解”埮生物による
環境浄化研究報告参照。そこで発明者等は、セ
ルロヌス分解菌培逊の基質調補法に適甚できるず
考え、セルロヌス性物質を氎に懞濁しオゟンを吹
き蟌みオゟン凊理を行぀た。しかし、セルロヌス
分解菌は、セルロヌス性物質䞭のセルロヌスをほ
ずんど資化しなか぀た。これはセルロヌス性物質
䞭のリグニンは、廃液リグニンのような溶解性リ
グニンず異なり、立䜓的な䞉次構造をずるこずか
ら、䞊蚘報告の方匏ではセルロヌス性物質のリグ
ニンはオゟンにより分解されにくいず掚定され
た。そこで、発明者等は、セルロヌス性物質のオ
ゟン凊理をさらに皮々怜蚎を重ねた結果、セルロ
ヌス性物質を含氎させお、オゟンず気固接觊させ
特定量以䞊のオゟンず反応させるこずにより、セ
ルロヌス分解はセルロヌス性物質䞭のセルロヌス
を良く分解するこずを芋出しお、本発明に到぀
た。
It has been reported that lignin is decomposed by ozone treatment of the lignin waste liquid discharged from the wood pulping process in the paper industry (1975 Ministry of Education specific research, Takamasa Higuchi, “Reducing waste liquid lignin by ozone and microbial treatment”). "Decomposition": see research report on environmental purification using microorganisms). Therefore, the inventors thought that this method could be applied to a substrate preparation method for culturing cellulose-degrading bacteria, and carried out ozone treatment by suspending a cellulosic substance in water and blowing ozone into it. However, cellulose-degrading bacteria hardly utilized cellulose in cellulosic substances. This is because the lignin in cellulosic substances has a three-dimensional tertiary structure, unlike soluble lignin such as waste liquid lignin, so it is assumed that the lignin in cellulosic substances is difficult to be decomposed by ozone using the method reported above. Ta. Therefore, as a result of further studies on ozone treatment of cellulosic materials, the inventors discovered that cellulose decomposition can be prevented by immersing cellulosic materials in water, bringing them into gas-solid contact with ozone, and reacting with more than a specific amount of ozone. The present invention was achieved by discovering that cellulose in cellulosic substances can be effectively decomposed.

以䞋、実斜䟋に埓぀お本発明を説明する。 The present invention will be described below with reference to Examples.

本発明者等は、䞋蚘装眮を甚いお、セルロヌス
性物質のオゟン凊理及び、オゟン凊理したセルロ
ヌス性物質のセルロヌス分解菌による資化性に぀
いお倚角的に怜蚎した。
The present inventors conducted a multifaceted study on ozone treatment of cellulosic materials and assimilation of the ozonated cellulosic materials by cellulose-degrading bacteria using the following apparatus.

第図は、本発明で䜿甚した培逊装眮の抂略図
であり、はセルロヌス性物質、即ち原料、は
以倖を含む氎溶性の培地、は混合機、はオ
ゟン凊理槜、は移動局、はオゟン吹き蟌み
口、はオゟン発生装眮、は空気、は排出フ
むダヌ、は殺菌管、は蒞気、は培逊
槜及びは排出口を瀺す。
FIG. 1 is a schematic diagram of the culture apparatus used in the present invention, in which 1 is a cellulosic substance, that is, a raw material, 2 is a water-soluble medium containing other than 1, 3 is a mixer, 4 is an ozone treatment tank, 5 1 is a moving bed, 6 is an ozone inlet, 7 is an ozone generator, 8 is air, 9 is a discharge feeder, 10 is a sterilization tube, 11 is steam, 12 is a culture tank, and 13 is a discharge port.

本装眮は、たず図瀺のようにセルロヌス性物質
である原料ず炭玠源を含たぬ培地ずを混合機
で混合し、次いでオゟン凊理槜でオゟンず反
応される。ここで培地は、硫安や塩安などの無
機窒玠及びリン酞塩、マグネシりム塩、カリりム
塩、などの無機塩を含む氎溶液である。たた、培
地は単に氎だけでも良いが、この堎合は、埌段
で改めお䞊蚘培地組成物を添加すればよい。なお
セルロヌス分解菌が有機窒玠やビタミン類を芁求
する堎合は、オゟン反応埌に添加すれば良い。混
合機ではセルロヌス性物質の原料は含氎率が
90以䞋に調補される。この原料は、オゟン凊
理槜内で槜底郚のオゟン吹き蟌み口から䟛絊
されるオゟンず接觊する。なお、オゟンは、オゟ
ン発生装眮により空気を原料ずしお調補され
る。このずきの入口オゟン濃床は、0.1〜20
m3であれば良いが、特に限定するものではない。
オゟン反応槜内の原料は、槜底郚に蚭けられ
た排出フむダヌにより抜き出されるため、移動
槜ずな぀お䞋降する。このずき、䞊昇するオゟ
ンず向流接觊する。なおオゟン凊理槜は、機械
的に原料を撹拌し、オゟンず接觊させる装眮で
も良い。
In this apparatus, first, as shown in the figure, a raw material 1 which is a cellulosic substance and a medium 2 containing no carbon source are mixed in a mixer 3, and then reacted with ozone in an ozone treatment tank 4. Here, the medium 2 is an aqueous solution containing inorganic nitrogen such as ammonium sulfate and ammonium chloride, and inorganic salts such as phosphate, magnesium salt, and potassium salt. Further, the medium 2 may be simply water, but in this case, the above-mentioned medium composition may be added again at a later stage. Note that if cellulose-degrading bacteria require organic nitrogen or vitamins, they may be added after the ozone reaction. In the mixer 3, the moisture content of the cellulosic substance raw material 1 is
Prepared to 90% or less. This raw material 1 comes into contact with ozone supplied from an ozone blowing port 6 at the bottom of the tank in the ozone treatment tank 4 . Note that ozone is prepared by an ozone generator 7 using air 8 as a raw material. The inlet ozone concentration at this time is 0.1 to 20g/
m 3 is sufficient, but there is no particular limitation.
The raw material 5 in the ozone reaction tank 4 is extracted by a discharge feeder 9 provided at the bottom of the tank, and thus becomes a moving tank 5 and descends. At this time, it comes into countercurrent contact with the rising ozone. Note that the ozone treatment tank 4 may be a device that mechanically stirs the raw material 5 and brings it into contact with ozone.

オゟン凊理槜でオゟン凊理された原料は、
排出フむダヌにより抜き出され、殺菌管に
入る。殺菌管は蒞気により100℃皋床に
加熱される。そしお殺菌管を通過した原料
は、殺菌されるず同時に未反応のオゟンが分解さ
れる。なお、殺菌方法ずしおは、特に限定しな
い。
The raw material 5 that has been ozonated in the ozone treatment tank 4 is
It is extracted by the discharge feeder 9 and enters the sterilization tube 10. The sterilization tube 10 is heated to about 100° C. by the steam 11. Then, the raw material 5 passed through the sterilization pipe 10
is sterilized and at the same time unreacted ozone is decomposed. Note that the sterilization method is not particularly limited.

殺菌された原料は、培逊槜に䟛絊され
る。培逊槜内では、原料ずセルロヌス分解
菌ずが混合される。そしお原料䞭のセルロヌス
は、セルロヌス分解菌の分泌するセルラヌれセ
ルロヌス加氎分解酵玠により䜎分子化される。
なお培逊方匏は、固䜓培逊あるいは液内培逊方匏
どちらでも良い。このずき培逊槜内は、セル
ロヌス分解菌の生育に適した条件、䟋えば、枩床
やPHなどが最適倀にコントロヌルする必芁があ
る。たた、セルロヌス分解菌は、Cellulomans
属Cellribrio属Pseudomonas属Clostrdium
属Actinomyces属Aspergillus属
Penicillium属、などのセルロヌス分解胜のある
菌を甚いるこずができず、特に限定するものでな
い。
The sterilized raw material 5 is supplied to the culture tank 12. In the culture tank 12, the raw material 5 and cellulose-degrading bacteria are mixed. The cellulose in the raw material 5 is reduced in molecular weight by cellulase (cellulose hydrolase) secreted by cellulose-degrading bacteria.
The culture method may be either a solid culture method or a submerged culture method. At this time, conditions in the culture tank 12 that are suitable for the growth of cellulose-degrading bacteria, such as temperature and pH, must be controlled to optimal values. In addition, cellulose-degrading bacteria are Cellulomans
Genus, Cellribrio, Pseudomonas, Clostrdium
Genus, Actinomyces, Aspergillus,
Bacteria capable of decomposing cellulose, such as those of the genus Penicillium, cannot be used, and there are no particular limitations.

分解生成物、分解残枣及びセルロヌス分解菌の
混合物は、排出口より取り出される。
A mixture of decomposition products, decomposition residues, and cellulose-degrading bacteria is taken out from the outlet 13.

次に本発明の実斜䟋により説明するが、本発明
は、これによりなんら限定されるものではない。
Next, the present invention will be explained with reference to Examples, but the present invention is not limited thereto.

実斜䟋  倩日也燥した皲わらを〜10mmに切断したもの
を培地ず混合し、含氎率〜85重量の皲わらを
調補した。なお、培地は塩化ナトリりム6.0
硫酞アンモニりム1.0リン酞䞀カリ
りム0.5リン酞二カリりム0.5硫
酞マグネシりム0.2塩化カルシりム0.3
の氎溶液ずした。この皲わらを前蚘オゟン
凊理槜内に投入しオゟンずの気―固接觊反応を行
぀た。なお、吹き蟌みオゟン濃床は12m3ずし
た。たた反応枩床は宀枩ずした。オゟン反応量
は、入口ず出口のオゟン濃床差、オゟン吹き蟌み
速床及び接觊時間ずから算出した。オゟン反応量
の単䜍は、也燥皲わら圓りに反応したオゟン
の重量である。
Example 1 Sun-dried rice straw was cut into 5-10 mm pieces and mixed with a culture medium to prepare rice straw with a moisture content of 5-85% by weight. The medium contains 6.0g of sodium chloride/
, ammonium sulfate 1.0g/, monopotassium phosphate 0.5g/, dipotassium phosphate 0.5g/, magnesium sulfate 0.2g/, calcium chloride 0.3
g/aqueous solution. This rice straw was placed in the ozone treatment tank and subjected to gas-solid contact reaction with ozone. Note that the ozone concentration blown was 12 g/m 3 . Moreover, the reaction temperature was room temperature. The amount of ozone reaction was calculated from the difference in ozone concentration between the inlet and the outlet, the ozone blowing rate, and the contact time. The unit of ozone reaction amount is the weight of ozone reacted per 1 g of dry rice straw.

第図に枬定結果を瀺す。のプロツトが、本
実斜䟋の結果である。皲わらに無機窒玠や無機塩
を含む氎溶性培地を添加しおも、皲わらずオゟン
ずが反応し、含氎率の増加に埓぀おオゟン反応量
が増加した。ここで比范䟋ずしお、氎を含氎させ
た皲わらに぀いお、同様の凊理を行぀た。その結
果を第図に䜵蚘した。のプロツトは、比范䟋
の結果である。比范䟋ず䞊蚘実斜䟋の結果より、
氎溶性の培地を甚いおも、氎ずほずんど同様の結
果が埗られるこずがわか぀た。なお、含氎率70重
量以䞊でオゟン反応量が枛少したのは、皲わら
盞互の付着により、オゟンずの接觊効率が䜎䞋す
るためである。
Figure 2 shows the measurement results. Plot A is the result of this example. Even when a water-soluble medium containing inorganic nitrogen and inorganic salts was added to rice straw, the rice straw reacted with ozone, and the amount of ozone reaction increased as the water content increased. As a comparative example, rice straw soaked with water was subjected to the same treatment. The results are also shown in Figure 2. Plot B is the result of a comparative example. From the results of the comparative example and the above example,
It was found that almost the same results as with water can be obtained using a water-soluble medium. The reason why the amount of ozone reaction decreased when the water content was 70% by weight or more was because the rice straws adhered to each other, reducing the efficiency of contact with ozone.

実斜䟋  前蚘実斜䟋で埗られたオゟン凊理皲わらを基
質ずしおセルロヌス分解菌の菌培を行぀た。
Example 2 Cellulose-degrading bacteria were cultured using the ozonated rice straw obtained in Example 1 as a substrate.

セルロヌス分解菌ずしおは、Trichoderma
virideアメリカン・タむプ・カルチナアヌ・コ
レクシペンATCCNo.13631及びコンポスト
堆肥から分離した菌株末同定、仮称CNY―
226株を甚いた。培逊は、固䜓培逊方匏ずし、
すなわち湿最状態でオゟン凊理皲わらずセルロヌ
ス分解菌を奜気的に混合した。なお、䞡菌株は、
ビタミンを芁求するこずから、培逊にあたり予じ
め殺菌しおおいた酵母゚キス溶液をオゟン凊理皲
わらに添加した。たた培逊枩床は、
Trichoderma virideは30℃CNY―266株は50
℃ずした。
Trichoderma is a cellulose-degrading bacterium.
viride (American Type Culture Collection: ATCC No. 13631) and a bacterial strain isolated from compost (final identification, tentative name CNY-
226 strains) were used. Cultivation is done using a solid culture method.
That is, ozonated rice straw and cellulose-degrading bacteria were mixed aerobically in a moist state. In addition, both strains are
Since the yeast requires vitamins, a previously sterilized yeast extract solution was added to the ozone-treated rice straw for cultivation. In addition, the culture temperature is
30℃ for Trichoderma viride, 50℃ for CNY-266 strain
℃.

第図に、含氎率ず菌䜓生成量ずを瀺した。培
逊時間は日ずした。は、Trichoderma
virideはCNY―226株の堎合を瀺す。なお、
含氎率重量のプロツトは、オゟン凊理しない
堎合である。図から含氎率が増加するに埓぀お、
菌䜓生成量が増加しおおり、実斜䟋ず同様な結
果が埗られた。この点から、オゟン反応量が菌䜓
生成量を巊右しおいる因子ず考えられる。すなわ
ち、オゟン反応量が倚くなるず、皲わら䞭のセル
ロヌスがセルロヌス分解菌により資化され易くな
るず考えられるずころで、含氎率が70重量以䞊
では、オゟン反応量は含氎率10重量より倧きい
のにかかわらず、菌䜓生成量が少ない。特に含氎
率90重量付近では、菌䜓生成量はほずんど無凊
理のものず同じであ぀た。この原因は次のように
考えられる。含氎率70重量以䞊の皲わらを調補
する堎合、遊離の氎が倚く、しかもその遊離氎は
可溶性物質を含み、か぀色を呈した。しかし、オ
ゟンで凊理するずほが脱色された。このこずか
ら、䞊蚘原因はオゟンが皲わらず盎接反応せず、
皲わらの溶出物ず反応しおしたうためであり、そ
の結果、実質的にオゟン凊理の効果が珟われなか
぀たず掚定した。
FIG. 3 shows the moisture content and the amount of bacterial cells produced. The culture time was 8 days. C is for Trichoderma
viride, D shows the case of CNY-226 strain. In addition,
The plot with a moisture content of 0% by weight is the case without ozone treatment. From the figure, as the water content increases,
The amount of bacterial cells produced increased, and the same results as in Example 1 were obtained. From this point of view, the amount of ozone reaction is considered to be a factor that influences the amount of bacterial cell production. In other words, it is thought that as the amount of ozone reaction increases, the cellulose in rice straw becomes more easily assimilated by cellulose-degrading bacteria, and when the water content is 70% by weight or more, the amount of ozone reaction is greater than the water content of 10% by weight. Regardless, the amount of bacteria produced is small. In particular, when the water content was around 90% by weight, the amount of bacterial cells produced was almost the same as that of the untreated sample. The reason for this is thought to be as follows. When rice straw with a moisture content of 70% by weight or more was prepared, there was a large amount of free water, and the free water contained soluble substances and had a color. However, when treated with ozone, most of the color was removed. From this, the above cause is that ozone does not react directly with rice straw,
It is assumed that this is because the ozonation reacts with the eluate of the rice straw, and as a result, the effect of ozonation treatment is virtually ineffective.

以䞊の結果から刀断し、実質的にオゟン凊理の
効果を埗るには、含氎率を90重量以䞋にすべき
である。
Judging from the above results, in order to substantially obtain the effect of ozone treatment, the water content should be 90% by weight or less.

実斜䟋  オゟン反応量が〜0.04―オゟン―也燥皲
わらの皲わらを調補し、Trichoderma viride
CNY―226株、及びCellulomonas flavigena
ATCCNo.484の培逊を行぀た。なお、
Tichoderma viride及びCNY―226株は固䜓培
逊で、Cellulomonas flavigenaの培逊は液䜓培
逊ずした。
Example 3 Rice straw with an ozone reaction amount of 0 to 0.04-ozone/g-dried rice straw was prepared, and Trichoderma viride,
CNY-226 strain and Cellulomonas flavigena
(ATCC No. 484) was cultured. In addition,
Tichoderma viride and CNY-226 strains were cultured in solid state, and Cellulomonas flavigena was cultured in liquid culture.

なお、Cellulomonas flavigenaの培逊では、
枩床30℃でPHを6.8にコントロヌルした。
In addition, in the culture of Cellulomonas flavigena,
The temperature was 30°C and the pH was controlled at 6.8.

培逊10日目の結果をオゟン反応量で敎理したず
ころ第図のようにな぀た。はTrichoderma
virideはCNY―226株、及びは
Cellulomonas flavigenaの堎合を瀺す。
When the results on the 10th day of culture were organized by the amount of ozone reaction, the results were as shown in Figure 4. E is for Trichoderma
viride, F is CNY-226 stock, and G is
The case of Cellulomonas flavigena is shown.

第図よりオゟン反応量が増加するに埓぀お、
菌䜓生成量が増加しおいるこずがわかる。すなわ
ち、オゟン反応量が増加するに䌎い、皲わら䞭の
セルロヌスがセルロヌス分解菌により分解され易
くなるこずがわか぀た。特にオゟン反応量が
0.005―オゟン―也燥皲わら以䞊の皲わら
で、菌䜓生成量が著しく増加した。
From Figure 4, as the amount of ozone reaction increases,
It can be seen that the amount of bacterial cells produced is increasing. In other words, it was found that as the amount of ozone reaction increased, cellulose in rice straw became more easily decomposed by cellulose-degrading bacteria. In particular, the amount of ozone reaction
The amount of bacteria produced increased significantly with rice straw containing 0.005g-ozone/g-dry rice straw or higher.

以䞊の実斜䟋より、オゟン凊理の効果を実質的
に埗るには、セルロヌス性物質の含氎率を90以
䞋ずし、オゟンずの気―固接觊反応を行わしめ、
たたそのオゟン反応量を0.005――也燥皲
わら以䞊ずすれば良いず結論した。
From the above examples, in order to substantially obtain the effect of ozone treatment, the water content of the cellulosic material should be 90% or less, and a gas-solid contact reaction with ozone should be carried out.
It was also concluded that the amount of ozone reaction should be set to 0.005 g/g of dry rice straw or more.

セルロヌス性物質を炭玠源ずし、セルロヌス分
解菌を培逊し、䟋えば、菌䜓を埮生物蛋癜ずしお
生産する堎合、たたセルロヌス分解菌の分泌する
セルラヌれや有機酞を生産する堎合などにおいお
本発明を適甚すれば、セルロヌス性物質䞭のセル
ロヌスは、効率的にセルロヌス分解菌により分解
され生産率が向䞊する。たた本発明は、セルロヌ
ス性物質ずオゟンずの気―固接觊反応であるた
め、カセむ゜ヌダ凊理のような廃液凊理の問題も
生じない。たた、少ない消費オゟン反応量で凊理
効果が埗られおいるこずから、経枈的である。
If the present invention is applied, for example, when cellulose substances are used as a carbon source and cellulose-degrading bacteria are cultured to produce microbial proteins from the bacterial cells, or when cellulase or organic acids secreted by cellulose-degrading bacteria are produced, etc. The cellulose in the cellulosic material is efficiently decomposed by cellulose-degrading bacteria, improving the production rate. Furthermore, since the present invention involves a gas-solid contact reaction between a cellulosic substance and ozone, there is no problem in waste liquid treatment such as in caustic soda treatment. Furthermore, since the treatment effect is obtained with a small amount of consumed ozone reaction, it is economical.

【図面の簡単な説明】[Brief explanation of the drawing]

第図は本発明で甚いた培逊装眮の抂略図、第
図はオゟン反応量ず含氎率の関係を瀺すグラ
フ、第図は含氎率ず菌䜓生成量の関係を瀺すグ
ラフ、第図はオゟン反応量ず菌䜓生成量ずの関
係を瀺すグラフである。   原料、  培地、  混合機、 
 オゟン凊理槜、  移動槜、  オゟン吹
き蟌み口、  オゟン発生装眮、  空気、
  排出フむダヌ、  殺菌管、  
蒞気、  培逊槜、  排出口。
Figure 1 is a schematic diagram of the culture apparatus used in the present invention, Figure 2 is a graph showing the relationship between ozone reaction amount and water content, Figure 3 is a graph showing the relationship between water content and bacterial cell production, and Figure 4 is a graph showing the relationship between water content and bacterial cell production. The figure is a graph showing the relationship between the amount of ozone reaction and the amount of bacterial cell production. 1... Raw material, 2... Culture medium, 3... Mixer, 4...
... Ozone treatment tank, 5 ... Mobile tank, 6 ... Ozone blowing port, 7 ... Ozone generator, 8 ... Air,
9... Discharge feeder, 10... Sterilization tube, 11...
Steam, 12...Culture tank, 13...Outlet.

Claims (1)

【特蚱請求の範囲】  セルロヌス性物質を炭玠源ずしおセルロヌス
分解菌の培逊にあたり、セルロヌス性物質の含氎
率が90以䞋になるように無機窒玠及び無機塩を
含有する氎溶液ずを混合し、次いでオゟンず気固
接觊させるこずを特城ずするセルロヌス分解菌培
逊方法。  セルロヌス性物質ずオゟンを該セルロヌス性
物質の也燥重量に察しおオゟン反応量玄
0.005以䞊の割合で接觊させる特蚱請求の範囲
第項蚘茉のセルロヌス分解菌培逊方法。
[Claims] 1. When culturing cellulose-degrading bacteria using a cellulosic substance as a carbon source, the cellulosic substance is mixed with an aqueous solution containing inorganic nitrogen and inorganic salts so that the water content is 90% or less, and then A method for culturing cellulose-degrading bacteria, which is characterized by bringing the cellulose-degrading bacteria into gas-solid contact with ozone. 2 Cellulosic material and ozone are mixed in an amount of ozone reaction per 1 g of dry weight of the cellulosic material.
The method for culturing cellulose-degrading bacteria according to claim 1, wherein the cellulose-degrading bacteria are brought into contact at a rate of 0.005 g or more.
JP6392780A 1980-05-16 1980-05-16 Cultivating method for microorganism capable of hydrolyzing cellulose Granted JPS56160989A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6392780A JPS56160989A (en) 1980-05-16 1980-05-16 Cultivating method for microorganism capable of hydrolyzing cellulose

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6392780A JPS56160989A (en) 1980-05-16 1980-05-16 Cultivating method for microorganism capable of hydrolyzing cellulose

Publications (2)

Publication Number Publication Date
JPS56160989A JPS56160989A (en) 1981-12-11
JPS6319150B2 true JPS6319150B2 (en) 1988-04-21

Family

ID=13243458

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6392780A Granted JPS56160989A (en) 1980-05-16 1980-05-16 Cultivating method for microorganism capable of hydrolyzing cellulose

Country Status (1)

Country Link
JP (1) JPS56160989A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0244159A (en) * 1988-08-05 1990-02-14 Mitsubishi Electric Corp Refrigerator

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0244159A (en) * 1988-08-05 1990-02-14 Mitsubishi Electric Corp Refrigerator

Also Published As

Publication number Publication date
JPS56160989A (en) 1981-12-11

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