JPH022900A - Method for culturing anaerobes - Google Patents
Method for culturing anaerobesInfo
- Publication number
- JPH022900A JPH022900A JP63146084A JP14608488A JPH022900A JP H022900 A JPH022900 A JP H022900A JP 63146084 A JP63146084 A JP 63146084A JP 14608488 A JP14608488 A JP 14608488A JP H022900 A JPH022900 A JP H022900A
- Authority
- JP
- Japan
- Prior art keywords
- soln
- cellulose
- anaerobes
- culture
- methane
- 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.)
- Pending
Links
- 238000000034 method Methods 0.000 title claims abstract description 10
- 238000012258 culturing Methods 0.000 title claims abstract description 7
- 239000001913 cellulose Substances 0.000 claims abstract description 21
- 229920002678 cellulose Polymers 0.000 claims abstract description 21
- 230000000694 effects Effects 0.000 claims abstract description 6
- 235000013343 vitamin Nutrition 0.000 claims abstract description 6
- 239000011782 vitamin Substances 0.000 claims abstract description 6
- 229940088594 vitamin Drugs 0.000 claims abstract description 6
- 229930003231 vitamin Natural products 0.000 claims abstract description 6
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims abstract description 4
- 229910052760 oxygen Inorganic materials 0.000 claims abstract description 4
- 239000001301 oxygen Substances 0.000 claims abstract description 4
- 241001148471 unidentified anaerobic bacterium Species 0.000 claims description 15
- 239000000126 substance Substances 0.000 claims description 5
- 239000007864 aqueous solution Substances 0.000 claims description 4
- 239000000243 solution Substances 0.000 claims description 4
- 239000000470 constituent Substances 0.000 claims description 3
- 238000000354 decomposition reaction Methods 0.000 claims description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 abstract description 36
- 238000000855 fermentation Methods 0.000 abstract description 13
- 230000004151 fermentation Effects 0.000 abstract description 13
- 239000007789 gas Substances 0.000 abstract description 10
- 239000010802 sludge Substances 0.000 abstract description 5
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 abstract description 4
- 239000000463 material Substances 0.000 abstract description 3
- 150000003722 vitamin derivatives Chemical class 0.000 abstract description 3
- 229910002092 carbon dioxide Inorganic materials 0.000 abstract description 2
- 239000001569 carbon dioxide Substances 0.000 abstract description 2
- 239000002699 waste material Substances 0.000 abstract description 2
- 239000008246 gaseous mixture Substances 0.000 abstract 1
- 239000000758 substrate Substances 0.000 description 13
- 239000001963 growth medium Substances 0.000 description 5
- 229910052500 inorganic mineral Inorganic materials 0.000 description 4
- 235000010755 mineral Nutrition 0.000 description 4
- 239000011707 mineral Substances 0.000 description 4
- 230000007423 decrease Effects 0.000 description 3
- 238000006460 hydrolysis reaction Methods 0.000 description 3
- 229920005610 lignin Polymers 0.000 description 3
- 238000009790 rate-determining step (RDS) Methods 0.000 description 3
- PLXBWHJQWKZRKG-UHFFFAOYSA-N Resazurin Chemical compound C1=CC(=O)C=C2OC3=CC(O)=CC=C3[N+]([O-])=C21 PLXBWHJQWKZRKG-UHFFFAOYSA-N 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 244000144972 livestock Species 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- 230000001954 sterilising effect Effects 0.000 description 2
- 238000004659 sterilization and disinfection Methods 0.000 description 2
- 239000011573 trace mineral Substances 0.000 description 2
- 235000013619 trace mineral Nutrition 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- IOCJWNPYGRVHLN-MMALYQPHSA-N (2r)-2-amino-3-[[(2r)-2-amino-2-carboxyethyl]disulfanyl]propanoic acid;hydrochloride Chemical compound Cl.OC(=O)[C@@H](N)CSSC[C@H](N)C(O)=O IOCJWNPYGRVHLN-MMALYQPHSA-N 0.000 description 1
- 241000894006 Bacteria Species 0.000 description 1
- 102000057297 Pepsin A Human genes 0.000 description 1
- 108090000284 Pepsin A Proteins 0.000 description 1
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 1
- UCKMPCXJQFINFW-UHFFFAOYSA-N Sulphide Chemical compound [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 230000005587 bubbling Effects 0.000 description 1
- 229940041514 candida albicans extract Drugs 0.000 description 1
- 230000001461 cytolytic effect Effects 0.000 description 1
- 235000014113 dietary fatty acids Nutrition 0.000 description 1
- 239000000194 fatty acid Substances 0.000 description 1
- 229930195729 fatty acid Natural products 0.000 description 1
- 150000004665 fatty acids Chemical class 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000002609 medium Substances 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 229940111202 pepsin Drugs 0.000 description 1
- 102000004169 proteins and genes Human genes 0.000 description 1
- 108090000623 proteins and genes Proteins 0.000 description 1
- 239000007858 starting material Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
- 239000002023 wood Substances 0.000 description 1
- 239000012138 yeast extract Substances 0.000 description 1
Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
Landscapes
- Micro-Organisms Or Cultivation Processes Thereof (AREA)
- Treatment Of Sludge (AREA)
Abstract
Description
【発明の詳細な説明】
A、産業上の利用分野
本発明はメタン発酵に用いられる嫌気性菌群の培養方法
に関するものである。DETAILED DESCRIPTION OF THE INVENTION A. Field of Industrial Application The present invention relates to a method for culturing anaerobic bacteria used in methane fermentation.
B9発明の概要
本発明は嫌気性菌群を培養する方法において、生物体の
構成物質、セルロース及びビタミンを含む培養液に嫌気
性菌群を含む例えば沼の底泥を接種して培養することに
より、
セルロースを分解してメタンを生成する能力の高い嫌気
性菌群を得ろことができるようにしたしのである。B9 Summary of the Invention The present invention provides a method for culturing anaerobic bacteria by inoculating, for example, swamp bottom mud containing anaerobic bacteria into a culture solution containing constituent substances of living organisms, cellulose, and vitamins. This made it possible to obtain a group of anaerobic bacteria that are highly capable of decomposing cellulose and producing methane.
C2従来の技術
汀機性廃棄物を処理する方法の一つとしてメタン発酵法
が知られている。この方法はメタン菌群を含む嫌気性菌
群により基質を一旦脂肪酸に分解し、更にこれを分解し
てメタンガスを得るらのである。この場合基質の種類に
より発酵速度が異なり、一般にメタン発酵の律速段階と
なるのは基質の加水分解反応またはメタン生成反応であ
る。Jl(質が易分解性6機物である場合にはメタン生
成反応が律速段階となるのに対し、基質が難分解性有機
物である場合には加水分解反応が律速段階となる。C2 Prior Art Methane fermentation is known as one of the methods for treating mechanical waste. In this method, a substrate is first decomposed into fatty acids by a group of anaerobic bacteria including a group of methane bacteria, and then this is further decomposed to obtain methane gas. In this case, the fermentation rate varies depending on the type of substrate, and generally the rate-limiting step in methane fermentation is the hydrolysis reaction of the substrate or the reaction to produce methane. When the substrate is an easily decomposable organic substance, the methane production reaction becomes the rate-limiting step, whereas when the substrate is a difficult-to-decompose organic substance, the hydrolysis reaction becomes the rate-limiting step.
D1発明が解決しようとする課題
ところで家畜の糞や排水の活性汚泥処理によって生じろ
余剰汚泥中にはセルロースが大量に含まれている。自然
界におlするセルロースには、木材に含まれろリタ′ニ
ンと結合したりクツセルロース渋びリグニンと結合して
いないセルロースかあり、リクノセルロースは難分解性
であって、そのままではメタン発酵の基質になりにくい
。ここで家畜の糞や余剰汚泥中に含まれるセルロースは
リグニンと結合していないものであり、メタン発酵の基
質になるか、加水分解の反応速度が遅い。従ってセルロ
ース含¥f率の高い基質においては、発酵速度が遅く、
白″機物m位量当たりのガス発生量が小さい。特に低温
下では微生物の活性が低下ずろためにセルロース系基質
の低温メタン発酵を実施ずろことが困難であった。D1 Problems to be Solved by the Invention Surplus sludge produced by activated sludge treatment of livestock excrement and wastewater contains a large amount of cellulose. Cellulose found in the natural world includes cellulose that is bound to lignin, which is contained in wood, and cellulose that is not bound to lignin. Lichnocellulose is difficult to decompose and cannot be used as it is for methane fermentation. Hard to become a substrate. The cellulose contained in livestock excrement and surplus sludge is not bound to lignin, so it either becomes a substrate for methane fermentation or has a slow hydrolysis reaction rate. Therefore, in substrates with high cellulose content, the fermentation rate is slow;
The amount of gas generated per meter of white material is small. Particularly at low temperatures, the activity of microorganisms decreases, making it difficult to carry out low-temperature methane fermentation of cellulosic substrates.
本発明の目的は、セルロース系基質に対してメタン生成
能力の高い嫌気性菌群を得ろことにある。An object of the present invention is to obtain a group of anaerobic bacteria that have a high ability to produce methane on cellulosic substrates.
E4課題を解決するための手段
本発明は、生物体の構成物質の水溶液にセル〔1−スと
ヒタミンとを加えると共に、その水溶液中から溶存酸素
を追い出して培養液を作製し、この培養液を用いて嫌気
性菌群を培養ずろことによりセルロース分解活性の高い
嫌気性菌I!1を選択的に得ることを特徴とする。E4 Means for Solving Problems The present invention involves adding cell [1-se] and hitamine to an aqueous solution of constituent substances of living organisms, and expelling dissolved oxygen from the aqueous solution to prepare a culture solution. By culturing a group of anaerobic bacteria using anaerobic bacteria I! 1 is selectively obtained.
F、実施例
本発明方法に用いられる嫌気性菌群の培養用培地のコ、
J整について述べると、先ず水にに、HPO。F. Example of a culture medium for anaerobic bacteria used in the method of the present invention,
When talking about J-sei, first of all, water and HPO.
をK 、 I(P O4のa度が6g/12になるよう
溶解して得たミネラルlと、表1〜表3に夫々成分を示
すミネラル2.トレースミネラル及びトレースビタミ/
を用αする。Mineral l obtained by dissolving K, I (P O4 so that the degree of a is 6 g/12, and minerals whose components are shown in Tables 1 to 3, respectively. 2. Trace minerals and trace vitamins /
Use α.
表 2
表 1
表
そして水860xQにミネラルI及びミネラル2各50
1.トレースミネラル1OruQを加え、Fe50.−
71−1.02y、Na1−IC0,5g、 レザズ
リンtmgを溶解する。次にセルロース(濾紙粉末)5
g、Yeast Extract (酵母抽出物) 2
g、 Tripticase Pcptomc (ペプ
シンによりタンパク質を途中まで分解した乙の)2gを
加えろ。オートクレーブで滅菌後、室温まで冷却し、N
、+CO,(80:20)混合ガスをバブリングしなが
ら表3のトレースビタミン101.システィン塩酸塩0
.59/rOmQ、、硫化ソーダ+9/2011Q、を
濾過滅菌して加えろ。培地中のレザズリンの色が消失し
て溶仔酸索が無くなったことを確認してから、前記混合
ガス気流下で適当な培養容器に移す。なお特殊な目的以
外は滅菌操作を行わなくても培養可能である。Table 2 Table 1 Table and 860xQ of water, 50 each of Mineral I and Mineral 2
1. Add trace mineral 1 OruQ, Fe50. −
Dissolve 71-1.02y, Na1-IC0.5g, and resazurin tmg. Next, cellulose (filter paper powder) 5
g, Yeast Extract 2
g. Add 2 g of Tripticase Pcptomc (from which the protein has been partially degraded with pepsin). After sterilization in an autoclave, cool to room temperature, and
, +CO, (80:20) while bubbling mixed gas, trace vitamin 101. of Table 3. Cystine hydrochloride 0
.. 59/rOmQ, filter sterilize and add Soda Sulfide + 9/2011Q. After confirming that the color of resazurin in the medium has disappeared and there are no molten acid cords, the culture medium is transferred to a suitable culture container under the above-mentioned mixed gas stream. It should be noted that culturing is possible without sterilization except for special purposes.
一方寒冷地の沼の底泥などから嫌気性菌群を含む汚泥を
採取しておき、これを培養容器内の培地に接種した後適
当な温度(15〜25℃)に保Aし、間欠的に撹拌を行
う。セルロースが分解してメタンガスと二酸化炭素ガス
が発生ずるが、基質の減少によりガス発生が低下してき
たら培養液を交換する。以上の操作を繰り返すことによ
りセルロース分解活性の高い嫌気性菌群が選択される。On the other hand, sludge containing anaerobic bacteria is collected from the bottom of a swamp in a cold region, inoculated into a culture medium in a culture container, kept at an appropriate temperature (15-25℃), and Stir. Cellulose decomposes and methane gas and carbon dioxide gas are generated, but when the gas generation decreases due to a decrease in substrate, replace the culture medium. By repeating the above operations, a group of anaerobic bacteria with high cellulose decomposition activity is selected.
このようにして得られた嫌気性菌群によりセルロース(
濾紙粉末)を含む打機性基質に対してメタン発酵を行っ
たところ、1日当たりタンク容積tCに対して0.5Q
のガスが発生し、従って発酵速度が速いことが確認され
た。なおこの実施例におけろ培地の組成を表4に示す。Cellulose (
When methane fermentation was carried out on a batter substrate containing (filter paper powder), 0.5Q per day per tank volume tC.
It was confirmed that gas was generated and therefore the fermentation rate was fast. The composition of the culture medium in this example is shown in Table 4.
表
G0発明の効果
本発明によれば、実施例の実験結果かられかるようにセ
ルロースを分解してメタンを生成する能力の高い培養系
を選択することができる。従って本発明方法により天竜
培養を行って得られた高セルロース分解活性嫌気性菌群
をセルロースを含む基質のメタン発酵プロセスにおいて
種菌として用いれば、馴養期間が短縮すると共に発酵の
処理効率を高めることが可能である。Table G0 Effects of the Invention According to the present invention, it is possible to select a culture system that has a high ability to decompose cellulose and produce methane, as seen from the experimental results in Examples. Therefore, if the highly cellulolytic anaerobic bacteria group obtained by Tenryu culture according to the method of the present invention is used as a starter in the methane fermentation process of a substrate containing cellulose, the acclimatization period can be shortened and the processing efficiency of fermentation can be increased. It is possible.
Claims (1)
ンとを加えると共に、その水溶液中から溶存酸素を追い
出して培養液を作製し、この培養液を用いて嫌気性菌群
を培養することによりセルロース分解活性の高い嫌気性
菌群を選択的に得ることを特徴とする嫌気性菌群の培養
方法。(1) Cellulose and vitamins are added to an aqueous solution of the constituent substances of living organisms, and dissolved oxygen is expelled from the aqueous solution to prepare a culture solution, and this culture solution is used to culture anaerobic bacteria. A method for culturing anaerobic bacteria, which is characterized by selectively obtaining anaerobic bacteria with high decomposition activity.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63146084A JPH022900A (en) | 1988-06-14 | 1988-06-14 | Method for culturing anaerobes |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63146084A JPH022900A (en) | 1988-06-14 | 1988-06-14 | Method for culturing anaerobes |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH022900A true JPH022900A (en) | 1990-01-08 |
Family
ID=15399762
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP63146084A Pending JPH022900A (en) | 1988-06-14 | 1988-06-14 | Method for culturing anaerobes |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH022900A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP2474374A1 (en) | 2005-10-28 | 2012-07-11 | Novelis Inc. | Homogenization and heat-treatment of cast metals |
-
1988
- 1988-06-14 JP JP63146084A patent/JPH022900A/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP2474374A1 (en) | 2005-10-28 | 2012-07-11 | Novelis Inc. | Homogenization and heat-treatment of cast metals |
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