JPS6087898A - Methane fermentation device - Google Patents
Methane fermentation deviceInfo
- Publication number
- JPS6087898A JPS6087898A JP58195668A JP19566883A JPS6087898A JP S6087898 A JPS6087898 A JP S6087898A JP 58195668 A JP58195668 A JP 58195668A JP 19566883 A JP19566883 A JP 19566883A JP S6087898 A JPS6087898 A JP S6087898A
- Authority
- JP
- Japan
- Prior art keywords
- gas
- fermentation
- membrane filter
- polymer membrane
- 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
- Y02W10/10—Biological treatment of water, waste water, or sewage
-
- 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)
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
Abstract
Description
【発明の詳細な説明】
産業上の利用分野
本発明は有機性廃棄物を処理するメタン発酵装置に関す
るものである。DETAILED DESCRIPTION OF THE INVENTION Field of the Invention The present invention relates to a methane fermentation device for treating organic waste.
従来例の構成とその問題点
従来より、有機性廃棄物の処理のため、メタン発酵装置
は−、般家庭用をはじめ、食堂厨芥、a産廃棄物等を処
理する業務用にまで広く用いられてきた。しかし同装置
には結露水による管閉塞が生じるという不都合があった
。則ち、メタン発酵槽から発生する発酵ガスは、メタン
発酵槽温度の飽和蒸気圧の水分を含んでおり、温度の低
い配管部分で上記水分が結露し、配管中に多く溜った場
合、ガス流路を閉塞するという欠点があった。Conventional structure and its problems Traditionally, methane fermentation equipment has been widely used for processing organic waste, from household use to commercial use for processing cafeteria kitchen waste, agricultural waste, etc. It's here. However, this device had the disadvantage that condensed water caused pipe blockage. In other words, the fermented gas generated from the methane fermentation tank contains moisture at the saturated vapor pressure of the methane fermentation tank temperature, and if the moisture condenses in the piping section where the temperature is low and accumulates in the piping, the gas flow will be reduced. It had the disadvantage of blocking the road.
上記欠截を防ぐため、発酵ガス配管に傾斜をつけ、配管
最下部に補水器を設けて結露水を取除く方式が採られて
きた。しかし、この方式では、メタン発酵装置内のガス
配管がすべて傾斜配管となり、配管工事が繁雑で、かつ
外観上も不都合なだけでなく、装置内の各機器間をガス
配管が立体的に横切るため、メンテナンス時の障害とな
るという欠へかあった。In order to prevent the above-mentioned shortage, a method has been adopted in which the fermentation gas piping is sloped and a water supply device is installed at the bottom of the piping to remove condensed water. However, with this method, all the gas piping in the methane fermentation equipment is slanted piping, which not only makes the piping work complicated and inconvenient in terms of appearance, but also because the gas piping crosses three-dimensionally between each device in the equipment. However, there was a problem in that it became an obstacle during maintenance.
さらに、メタン発酵槽を寒冷地で使用する場合、上記傾
斜配管を設けても配管中に結露した水は配管中に氷着し
、配管を閉塞する欠点もあシ、寒冷地でも施工できるメ
タン発酵装置が望まれていた。Furthermore, when using a methane fermentation tank in a cold region, even if the above-mentioned inclined piping is installed, water that condenses in the piping may freeze and block the piping.Methane fermentation can be carried out even in cold regions. The device was desired.
発明の目的
本発明はかかる従来の欠点を解消し、配管が容易で寒冷
地でも施工可能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 eliminates such conventional drawbacks, and provides a methane fermentation device that has easy piping and can be installed even in cold regions.
発明の構成
本発明のメタン発酵装置は、メタン発酵槽のガス取出口
に、発酵ガス冷却器、活性炭濾過器および高分子膜濾過
器を順次気密的に接続し、メタン発酵槽から出る発酵ガ
スを上記3種の機器中を順次通過させるとともに、冷却
器および高分子膜濾過器に外気を供給してなるものであ
る。この構成により発酵ガス中の水分を効率よく除去す
るものである。Structure of the Invention The methane fermentation apparatus of the present invention connects a fermentation gas cooler, an activated carbon filter, and a polymer membrane filter in sequence to a gas outlet of a methane fermentation tank in an airtight manner, and collects fermentation gas from the methane fermentation tank. The outside air is passed sequentially through the above three types of equipment, and the outside air is supplied to the cooler and the polymer membrane filter. With this configuration, moisture in the fermentation gas can be efficiently removed.
実施例の説明 以下本発明の一実施例を図面と共に詳細に説明する。Description of examples An embodiment of the present invention will be described in detail below with reference to the drawings.
第1図において、1はメタン発酵槽2の上部に設けたガ
ス取出口、3はガス取出口1に連らなる発酵ガス冷却器
、4は発酵ガス冷却器3に接続した活性炭濾過器、5は
活性炭濾過器4内の活性炭層、6は2枚の樹脂膜7を枠
状のスペーサの両面に貼合せてその間に発酵ガスを供給
するようにした高分子膜濾過器で、活性炭濾過器4と連
絡している。そして上記各機器間の接続は気密性良く行
なわれている。8はガス配管接続口で、ガスタンク・ガ
スボイラー等発酵ガス消費装置に接続される。In FIG. 1, 1 is a gas outlet provided at the top of the methane fermentation tank 2, 3 is a fermentation gas cooler connected to the gas outlet 1, 4 is an activated carbon filter connected to the fermentation gas cooler 3, and 5 is a fermentation gas cooler connected to the fermentation gas cooler 3. 6 is an activated carbon layer in the activated carbon filter 4, and 6 is a polymer membrane filter in which two resin membranes 7 are pasted on both sides of a frame-shaped spacer to supply fermentation gas between them. I am in touch with you. The connections between the above-mentioned devices are made with good airtightness. 8 is a gas pipe connection port, which is connected to a fermentation gas consuming device such as a gas tank or gas boiler.
上記した水分を除去する高分子膜濾過器6および樹脂膜
7の高分子材料として、耐薬品性等を考慮し
F3
で代表されるようなパーフルオロスルホン酸樹脂(テト
ラフルオロエチレンとフルオロスルホニルモノマーの共
重合体で、以下PFSと称する)を用いた。このP F
S IJ′、水分透過率がメタンガス透過率より著し
く高く、常温で100〜1000倍である。As the polymer material for the polymer membrane filter 6 and the resin membrane 7 that remove the moisture mentioned above, in consideration of chemical resistance etc. A copolymer (hereinafter referred to as PFS) was used. This P F
S IJ', the water permeability is significantly higher than the methane gas permeability, which is 100 to 1000 times higher at room temperature.
次に本実施例装置の動作について説明する。メタン発酵
槽2内で発生した発酵ガスは矢印で示すように発酵ガス
冷却器3内へ入シ、外気温迄冷却される。メタン発酵槽
2内で約35°Cの消化液温下で100%R,H,の温
度をもつ発酵ガスは、発酵ガス冷却器3の出口で外気温
の100%R,H。Next, the operation of the apparatus of this embodiment will be explained. The fermentation gas generated in the methane fermentation tank 2 enters the fermentation gas cooler 3 as shown by the arrow and is cooled down to the outside temperature. The fermentation gas, which has a temperature of 100% R,H at the digestive fluid temperature of about 35°C in the methane fermentation tank 2, has a temperature of 100% R,H of the outside temperature at the exit of the fermentation gas cooler 3.
に冷却され、発酵ガス冷却器3内壁に過剰水分が結露す
る。上記結露水は発酵ガス冷却器3内壁からガス取出口
1を流下しメタン発酵槽2へ還流する。発酵ガス冷却器
3の出口より活性炭濾過器4に入った発酵ガスは、活性
炭層5を通り微量有害成分が除去される。活性炭濾過器
4を通過した発酵ガスは、高分子膜濾過器6に入り、水
分は樹脂膜7を通じ外部へ放散される。なお樹脂膜7お
よび発酵ガス冷却器3に外気が良く接する様にファン(
図示せず)を設けである。Excess moisture condenses on the inner wall of the fermentation gas cooler 3. The condensed water flows down from the inner wall of the fermentation gas cooler 3 through the gas outlet 1 and returns to the methane fermentation tank 2. The fermentation gas that enters the activated carbon filter 4 from the outlet of the fermentation gas cooler 3 passes through an activated carbon layer 5 to remove trace amounts of harmful components. The fermentation gas that has passed through the activated carbon filter 4 enters the polymer membrane filter 6, and moisture is released to the outside through the resin membrane 7. A fan (
(not shown) is provided.
高分子膜濾過器6の出口のガス配管接続口8よシ出た乾
燥された発酵ガスは、ガス配管を経てガスタンク、ガス
ボイラー等のガス消費機器へと送られる。The dried fermentation gas discharged from the gas pipe connection port 8 at the outlet of the polymer membrane filter 6 is sent to gas consuming equipment such as a gas tank and a gas boiler via a gas pipe.
次に第2図にもとづいて、本発明の他の実施例について
説明する。図において、9はコンプレッサー、エアタン
ク、アフタークーラ、ドレインセパレータおよび圧力調
整器等からなる乾燥加圧空気発生装置である。10はメ
タン発酵槽、11はメタン発酵槽10の上蓋部に取付け
られたガス取出口、12はガス取出口11に連らなる発
酵ガス冷却器、13は発酵ガス冷却器12中の熱交換器
、14は発酵ガス冷却器12に接続した活性炭濾過器で
内部には活性炭層21を設けている。15は高分子膜濾
過器で、その一端は高分子膜濾過器入口に接続されてい
る。そしてその構成は、PF3膜をチーーブ状に加工し
た脱炉材17と、その外側のポリプロピレン等のチーー
プ製の外覆チューブ18の二重のチューブより構成され
ている。19は高分子膜濾過器出口である。2oはガス
配管接続口、23は熱交換器13を経た乾燥加圧空気を
高分子膜濾過器15のp材17、外覆チー−ブ18間の
空隙22に導く配管である。Next, another embodiment of the present invention will be described based on FIG. In the figure, 9 is a dry pressurized air generating device consisting of a compressor, an air tank, an aftercooler, a drain separator, a pressure regulator, and the like. 10 is a methane fermentation tank, 11 is a gas outlet attached to the upper lid of the methane fermenter 10, 12 is a fermentation gas cooler connected to the gas outlet 11, and 13 is a heat exchanger in the fermentation gas cooler 12. , 14 is an activated carbon filter connected to the fermentation gas cooler 12, and an activated carbon layer 21 is provided inside. 15 is a polymer membrane filter, one end of which is connected to the inlet of the polymer membrane filter. The structure consists of a double tube including a de-furnacing material 17 made of a PF3 membrane processed into a chive shape, and an outer covering tube 18 made of cheap material such as polypropylene. 19 is a polymer membrane filter outlet. 2o is a gas pipe connection port, and 23 is a pipe that guides the dry pressurized air that has passed through the heat exchanger 13 to the gap 22 between the P material 17 and the covering tube 18 of the polymer membrane filter 15.
次に本実施例装置の動作について説明する。メタン発酵
槽10内で発生したガスは槽内消化液温と同温度で10
0%R,H,の温度の発酵ガスで、発酵ガス冷却器12
内へ導かれ外気温に冷却された後、活性炭濾過器14を
経て高分子膜濾過器入口16に達する。Next, the operation of the apparatus of this embodiment will be explained. The gas generated in the methane fermentation tank 10 is at the same temperature as the digestive fluid temperature in the tank.
Fermentation gas cooler 12 with fermentation gas at a temperature of 0% R, H.
After being guided into the interior and cooled to outside temperature, it passes through an activated carbon filter 14 and reaches a polymer membrane filter inlet 16.
一方、外気をコンプレッサーで約7 kcrf / c
ri程度に圧縮し、アフタクーラで外気温程度に冷却し
た後ドレンセパレータを通して乾燥した空気を作り、圧
力調整した後、発酵ガス冷却器12中の熱交換器13に
導く(矢印)。発酵ガスの温度と熱交換され昇温してさ
らに相対湿度の低下した空気は高分子膜濾過器出口19
から膜p材17と外覆チー−プ18との間に導かれる。Meanwhile, the outside air is compressed to about 7 kcrf/c
After being compressed to about ri and cooled to about the outside temperature using an aftercooler, dry air is created through a drain separator, the pressure is adjusted, and then introduced to the heat exchanger 13 in the fermentation gas cooler 12 (arrow). The air whose temperature has increased through heat exchange with the temperature of the fermentation gas and whose relative humidity has further decreased is sent to the polymer membrane filter outlet 19.
is introduced between the membrane p-material 17 and the sheathing chip 18.
膜p材17の内側には活性炭濾過器14を通過した発酵
ガスが流入しており、脱炉材17外側の乾燥空気と相対
するため、発酵ガス中の水分は脱炉材17を通じ乾燥空
気中へと拡散する。上記水分の拡散を行いながら高分子
膜濾過器出口19では発酵ガス中の水分は除去され、ガ
ス配管接続口20より他のガス機器に供給される。一方
、高分子膜濾過器出口19より脱炉材17の外側へ流入
した乾燥空気は湿気を含みながら高分子膜濾過器入1」
16より外気へ放出される。The fermented gas that has passed through the activated carbon filter 14 flows into the membrane p material 17 and faces the dry air outside the de-furnacing material 17, so that the moisture in the fermented gas passes through the de-furnacing material 17 into the dry air. spread to. While the moisture is being diffused, the moisture in the fermentation gas is removed at the polymer membrane filter outlet 19, and the fermented gas is supplied to other gas equipment through the gas piping connection port 20. On the other hand, the dry air flowing from the polymer membrane filter outlet 19 to the outside of the demolding material 17 enters the polymer membrane filter 1 while containing moisture.
16 to the outside air.
発明の効果
上記のように本発明は湿気を拡散するだめの空気流動に
要するエネルギー以外には大きな外部エネルギーを使用
する事なく発酵ガス中に含まれる水分を低減除去する事
ができるため、ガス配管中で結露水を生じる事がない。Effects of the Invention As mentioned above, the present invention can reduce and remove moisture contained in fermentation gas without using large amounts of external energy other than the energy required for air flow to diffuse moisture. There is no condensation water inside.
したがってガス配管を傾斜配管とする必要がないだめ配
管工事が簡略化され工事費、工事期間、工事部材等の削
減が可能となるだけでなく、メタン発酵装置運転中のメ
ンテナンスも簡素化され、立体配管が作業の障害となら
ない等の特長を有する。さらに発酵ガスを乾燥化させる
事により、ガス配管中での凍結も生じないため、寒冷地
でも容易にメタン発酵槽が施工運転できるという特長も
有する等、工業的価値は大である。Therefore, there is no need to make the gas piping an inclined pipe, which simplifies the piping work, which not only makes it possible to reduce construction costs, construction period, and construction materials, but also simplifies maintenance while the methane fermentation equipment is in operation. Features include that piping does not become an obstacle to work. Furthermore, by drying the fermentation gas, freezing does not occur in the gas pipes, so the methane fermentation tank can be easily constructed and operated even in cold regions, and has great industrial value.
第1図は本発明の一実施例装置の部分断面図、第2図は
他の実施例装置の部分断面図である。
3.12・・・・発酵ガス冷却器、4,14・・・・活
性炭濾過器、6,15・・・・・高分子膜濾過器。
代理人の氏名 弁理士 中 尾 敏 男 ほか1名第1
図FIG. 1 is a partial sectional view of an apparatus according to one embodiment of the present invention, and FIG. 2 is a partial sectional view of another embodiment of the apparatus. 3.12...Fermentation gas cooler, 4,14...Activated carbon filter, 6,15...Polymer membrane filter. Name of agent: Patent attorney Toshio Nakao and 1 other person No. 1
figure
Claims (1)
、活性炭洲過器および高分子膜濾過器を順次気密的に接
続し、前記メタン発酵槽〃・ら出る発酵ガスを上記3種
の機器中を順次通過させるとともに、冷却器および高分
子膜濾過器に外気を供給してなるメタン発酵装置。 (2)高分子膜濾過器として、パーフルオロスルホン酸
樹脂膜を用いた特許請求の範囲第1項記載のメタン発酵
装置。 (3)高分子膜濾過器として、2枚のパーフルオロスル
ホン酸樹脂膜により構成した特許請求の範囲第1項また
は第2項記載のメタン発酵装置。 (4)発酵ガス冷却器および高分子膜濾過器に外気を供
給する手段としてファンを設けてなる特許請求の範囲第
1項、第2項または第3項記載のメタン発酵装置。 (6)高分子膜濾過器をチーーブ状とした特許請求の範
囲第1項または第2項記載のメタン発酵装置。 (6)高分子膜濾過器を二重のチーープとし、両チーー
ブ間に外気を流通させてなる特許請求の範囲第1項、第
2項または第5項記載のメタン発酵装置。[Scope of Claims] (1) A fermentation gas cooler, an activated carbon filter, and a polymer membrane filter are sequentially and airtightly connected to the gas outlet of the methane fermentation tank, and the fermentation gas exiting from the methane fermentation tank is A methane fermentation device in which gas is sequentially passed through the three types of equipment described above, and outside air is supplied to a cooler and a polymer membrane filter. (2) The methane fermentation apparatus according to claim 1, which uses a perfluorosulfonic acid resin membrane as the polymer membrane filter. (3) The methane fermentation apparatus according to claim 1 or 2, wherein the polymer membrane filter is constituted by two perfluorosulfonic acid resin membranes. (4) The methane fermentation apparatus according to claim 1, 2 or 3, wherein a fan is provided as means for supplying outside air to the fermentation gas cooler and the polymer membrane filter. (6) The methane fermentation apparatus according to claim 1 or 2, wherein the polymer membrane filter is in the shape of a chive. (6) The methane fermentation apparatus according to claim 1, 2, or 5, wherein the polymer membrane filter is a double tube, and outside air is circulated between both tubes.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP58195668A JPS6087898A (en) | 1983-10-19 | 1983-10-19 | Methane fermentation device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP58195668A JPS6087898A (en) | 1983-10-19 | 1983-10-19 | Methane fermentation device |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS6087898A true JPS6087898A (en) | 1985-05-17 |
Family
ID=16345005
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP58195668A Pending JPS6087898A (en) | 1983-10-19 | 1983-10-19 | Methane fermentation device |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6087898A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0501376A2 (en) * | 1991-02-25 | 1992-09-02 | Heinrich Bauer | Plant for the production of biogas from manure |
US5681368A (en) * | 1995-07-05 | 1997-10-28 | Andrew Corporation | Dehumidifier system using membrane cartridge |
-
1983
- 1983-10-19 JP JP58195668A patent/JPS6087898A/en active Pending
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0501376A2 (en) * | 1991-02-25 | 1992-09-02 | Heinrich Bauer | Plant for the production of biogas from manure |
US5681368A (en) * | 1995-07-05 | 1997-10-28 | Andrew Corporation | Dehumidifier system using membrane cartridge |
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