JPS60197298A - Methane fermentation equipment - Google Patents
Methane fermentation equipmentInfo
- Publication number
- JPS60197298A JPS60197298A JP59052551A JP5255184A JPS60197298A JP S60197298 A JPS60197298 A JP S60197298A JP 59052551 A JP59052551 A JP 59052551A JP 5255184 A JP5255184 A JP 5255184A JP S60197298 A JPS60197298 A JP S60197298A
- Authority
- JP
- Japan
- Prior art keywords
- gas
- methane
- fermentation
- carbon dioxide
- methane fermentation
- 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
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
-
- 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
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/20—Sludge processing
Landscapes
- Treatment Of Sludge (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.
Description
【発明の詳細な説明】 産業上の利用分野 本発明はメタン発酵装置の改良に関するものである。[Detailed description of the invention] Industrial applications The present invention relates to improvements in methane fermentation equipment.
従来例の構成とその問題点
従来より、メタン発酵装置は農畜産家をはじめ、広く利
用されてきたが、微生物による反応を用いた装置である
ため、その保守管理は専門知識を必要とし難しい面があ
ったっ
即ち、メタン発酵装置ではメタン発酵槽から発生する発
酵ガスを燃焼させてエネルギーを取り出し、メタン発酵
槽の内部を加熱し、内部消化液中の微生物に最適生育条
件を作り出している。しかし、何らかの条件から消化液
の状態に変化をきたすと発酵ガスの組成が変化する。発
酵ガスは通常的60%のOH4と約40%のCO2より
構成される。一方、この発酵ガスを燃焼させるのに用い
るバーナーは、燃焼範囲の広いユニバーサルノ〈−ナー
を用いても、不燃性の002の濃度が約45%を上棚る
と継続した燃焼ができなくなるっこの事は、発酵ガスに
よる自己保温ができなくなり、消化液中の微生物の最適
生育条件の維持ができなくなり、結果として、さらにC
H4濃度を減少させるという悪循環を生じさせる。Conventional structure and problems Methane fermentation equipment has been widely used by farmers and livestock farmers, but because it uses microbial reactions, its maintenance requires specialized knowledge and is difficult. In other words, a methane fermentation device burns the fermentation gas generated from the methane fermentation tank to extract energy, heat the inside of the methane fermentation tank, and create optimal growth conditions for the microorganisms in the internal digestive fluid. However, if the state of the digestive fluid changes due to some condition, the composition of the fermentation gas changes. Fermentation gas typically consists of 60% OH4 and about 40% CO2. On the other hand, even if the burner used to combust this fermentation gas is a universal burner with a wide flammability range, if the concentration of non-flammable 002 exceeds about 45%, continuous combustion will not be possible. The problem is that the fermentation gas is no longer able to maintain its own heat, making it impossible to maintain optimal growth conditions for microorganisms in the digestive juices, and as a result, even more C.
This creates a vicious cycle of decreasing H4 concentration.
したがって、上記悪循環を引きおこさない、かつ保守管
理の容易なメタン発酵装置が望まれていた。Therefore, a methane fermentation device that does not cause the above-mentioned vicious cycle and is easy to maintain and manage has been desired.
発明の目的
本発明はか−る従来の欠点を克服し、保守管理の容易な
メタン発酵装置を提供するものである。OBJECTS OF THE INVENTION The present invention overcomes the drawbacks of the conventional method and provides a methane fermentation device that is easy to maintain and manage.
発明の構成
本発明は、メタン発酵槽から発生した発酵ガスの配管回
路中に炭酸ガス透過膜を具備するメタンガス濃縮装置を
設けた構成より成る。上記メタンガス濃縮装置は、炭酸
ガス透過膜の片面を発酵ガスに接するようにし、他面は
大気中に開放したものである。この構成により、発酵ガ
スを常に燃焼可能なメタン濃度に保つとともに保守管理
を容易にしだものである。Structure of the Invention The present invention has a structure in which a methane gas concentrator equipped with a carbon dioxide gas permeable membrane is provided in a piping circuit for fermentation gas generated from a methane fermentation tank. The above methane gas concentrator has a carbon dioxide gas permeable membrane with one side in contact with fermentation gas and the other side open to the atmosphere. This configuration allows the fermentation gas to always be maintained at a methane concentration that allows for combustion, and also facilitates maintenance and management.
実施例の説明
以下本発明の一実施例を添付図面と共に説明する。第1
図において1はメタン発酵槽、2はメタン発酵槽1と接
続された配管回路中に設けたメタン濃縮装置、3は濃縮
された発酵ガスを一時貯留し、かつ発酵ガス回路中のガ
スに圧力を附加するガスタンク、4はそのガス圧を検出
するガス圧力スイッチ、6は濃縮ガスを燃焼させるガス
ボイラー等のガス消9装置である。6はメタン濃縮装置
2の排気装置である。DESCRIPTION OF THE EMBODIMENTS An embodiment of the present invention will be described below with reference to the accompanying drawings. 1st
In the figure, 1 is a methane fermentation tank, 2 is a methane concentrator installed in a piping circuit connected to the methane fermentation tank 1, and 3 is a device that temporarily stores concentrated fermentation gas and applies pressure to the gas in the fermentation gas circuit. An additional gas tank, 4 a gas pressure switch for detecting the gas pressure, and 6 a gas extinguisher 9 such as a gas boiler for burning the concentrated gas. 6 is an exhaust device of the methane concentrator 2.
第2図はメタン濃縮装置2の部分断面図で、7は発酵ガ
スの出、入口、8は26μの担持体の上に約0.1μの
ジメチルシリコンをピンホールのない様にコーティング
した炭酸ガス透過膜、9は炭酸ガス透過膜8に均一な圧
力がかかるように圧力分散をはかる圧力分散層、10は
炭酸ガス透過膜8から透過した炭酸ガスをガス排出口1
1へ導ひくガス透過体で、連続発泡体で構成されている
。Figure 2 is a partial cross-sectional view of the methane concentrator 2, where 7 is the fermentation gas outlet and inlet, and 8 is carbon dioxide gas coated with about 0.1μ dimethyl silicone on a 26μ carrier without pinholes. A permeable membrane 9 is a pressure dispersion layer that distributes pressure so that a uniform pressure is applied to the carbon dioxide gas permeable membrane 8, and 10 is a gas discharge port 1 for transmitting carbon dioxide permeated from the carbon dioxide gas permeable membrane 8.
This is a gas permeable body that guides the gas to 1 and is made of open foam.
ガス排出口11は排気装置6と連絡しており、炭酸ガス
を吸引し、大気中に放出する。The gas outlet 11 communicates with the exhaust device 6, sucks in carbon dioxide gas, and releases it into the atmosphere.
次に本発明の一実施例の動作原理を説明する。Next, the operating principle of an embodiment of the present invention will be explained.
メタン発酵杓1で発生した発酵ガスは、メタン濃縮装置
2に入り、炭酸ガス透過膜8の表面に接する。炭酸ガス
透過膜8はジメチルシリコンよす構成されており、CO
2の透過係数は約300X10−10”4−8゜。、。The fermentation gas generated in the methane fermentation ladle 1 enters the methane concentrator 2 and comes into contact with the surface of the carbon dioxide permeable membrane 8. The carbon dioxide gas permeable membrane 8 is made of dimethyl silicone and is CO
The transmission coefficient of 2 is approximately 300X10-10"4-8°.
Iigに対しCH4の透過係数は約50X10”−’°
0c/、L、sea −cm H,9である。The permeability coefficient of CH4 for Iig is approximately 50X10"-'°
0c/, L, sea-cm H, 9.
そして炭酸ガス透過膜8の発酵ガス側には約150a+
zH20の圧力に保たれ、反対側は排気装置6により発
酵ガス圧に較べ約500 MM H,!?正圧力低く保
たれているため、発酵ガス中のCO2は炭酸ガス透過膜
8を透過しガス排出口11を経由し大気へ排出される。Approximately 150a+ is placed on the fermentation gas side of the carbon dioxide permeable membrane 8.
The pressure on the other side is maintained at a pressure of 20 mm H, compared to the fermentation gas pressure by the exhaust device 6. ? Since the positive pressure is kept low, CO2 in the fermentation gas passes through the carbon dioxide permeable membrane 8 and is discharged to the atmosphere via the gas discharge port 11.
一方メタンガスの大部分は出ロアからガスタンク3、ガ
ス消費装置6へ導かれる。On the other hand, most of the methane gas is led from the output lower to the gas tank 3 and the gas consumption device 6.
本実施例では30CrIL×30CrfLの炭酸ガス透
過膜8を2枚使用し、これを約−50ONllH,9の
排気装置6に接続した場合、常温下で約” ’/win
のC02を排出できた。なお、炭酸ガス透過膜8として
ジメチルシリコン薄膜を用いた例を示したが、同様な目
的を達成するものであればよく、ジメチルシリコン薄膜
に限られるものでないことはあきらかであるっ
発明の効果
上記のように本発明ではメタン濃縮装置をシステム中に
組込む事により、発酵ガスを常に燃焼可能なメタン濃度
に保つ事が可能となり、万一消化液中の微生物の生育状
態が変化して発酵ガス組成が変化しても自己保温が維持
でき、微生物の生育温度状態を悪化させ、生育条件をそ
れ以上くずす事がなく、微生物の自己回復力による生育
条件の適正化により元へ戻る事が可能となる。したがっ
て、専門家の知識を必要とせずメタン発酵装置の維持管
理ができる。さらにメタン濃縮に際し、炭酸ガス透過膜
を用いるため、そのだめの特別のメンテナンスを要しな
いという(Fj’Qもあり工業的価値は大である。In this embodiment, two carbon dioxide gas permeable membranes 8 of 30CrIL×30CrfL are used, and when these are connected to the exhaust device 6 of approximately -50ONllH,9, approximately "'/win at room temperature.
of CO2 could be emitted. Although an example is shown in which a dimethyl silicone thin film is used as the carbon dioxide gas permeable membrane 8, it is obvious that it is not limited to the dimethyl silicone thin film as long as it achieves the same purpose. In the present invention, by incorporating a methane concentrator into the system, it is possible to maintain the fermentation gas at a combustible methane concentration at all times, and in the unlikely event that the growth state of microorganisms in the digestive fluid changes and the fermentation gas composition changes. Even if the temperature changes, self-heat retention can be maintained, and the growth temperature condition of microorganisms will not deteriorate and the growth conditions will not deteriorate any further, and it will be possible to return to the original state by optimizing the growth conditions due to the self-healing power of microorganisms. . Therefore, the methane fermentation device can be maintained and managed without requiring the knowledge of experts. Furthermore, since a carbon dioxide gas-permeable membrane is used for methane concentration, no special maintenance is required (Fj'Q is also available, which is of great industrial value).
第1図は本発明の一実施例装置を示す概略構成図、第2
図は同装置のメタン濃縮装置を示す断面図である。
1・・・・・・メタン発酵槽、2・・・・・・メタン濃
縮装置、8・・・・・・炭酸ガス透過膜。
代理人の氏名 5μ理士 中 尾 敏 男 ほか1名第
1図
4
第 2 図FIG. 1 is a schematic configuration diagram showing an embodiment of the device of the present invention, and FIG.
The figure is a cross-sectional view showing the methane concentrator of the same device. 1... Methane fermentation tank, 2... Methane concentrator, 8... Carbon dioxide permeable membrane. Name of agent: Toshio Nakao, 5μ accountant, and one other person Figure 1 4 Figure 2
Claims (1)
ン濃縮装置を設け、このメタン濃縮装置は、片面を上記
発酵ガスに接し、他面を大気中に排気開放した炭酸ガス
透過膜を具備して成るメタン発酵装置。A methane concentrator is installed in the piping circuit for the fermentation gas generated from the methane fermentation tank, and the methane concentrator is equipped with a carbon dioxide permeable membrane having one side in contact with the fermentation gas and the other side open to the atmosphere. A methane fermentation device.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP59052551A JPS60197298A (en) | 1984-03-19 | 1984-03-19 | Methane fermentation equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP59052551A JPS60197298A (en) | 1984-03-19 | 1984-03-19 | Methane fermentation equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPS60197298A true JPS60197298A (en) | 1985-10-05 |
Family
ID=12917935
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP59052551A Pending JPS60197298A (en) | 1984-03-19 | 1984-03-19 | Methane fermentation equipment |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS60197298A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4834779A (en) * | 1986-10-27 | 1989-05-30 | Liquid Air Corporation | Process for membrane seperation of gas mixtures |
| JP2013538772A (en) * | 2010-07-09 | 2013-10-17 | エコ テクノル プロプライエタリー リミテッド | Generation of syngas by using membrane technology |
-
1984
- 1984-03-19 JP JP59052551A patent/JPS60197298A/en active Pending
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4834779A (en) * | 1986-10-27 | 1989-05-30 | Liquid Air Corporation | Process for membrane seperation of gas mixtures |
| JP2013538772A (en) * | 2010-07-09 | 2013-10-17 | エコ テクノル プロプライエタリー リミテッド | Generation of syngas by using membrane technology |
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