JPH0510160B2 - - Google Patents
Info
- Publication number
- JPH0510160B2 JPH0510160B2 JP58147035A JP14703583A JPH0510160B2 JP H0510160 B2 JPH0510160 B2 JP H0510160B2 JP 58147035 A JP58147035 A JP 58147035A JP 14703583 A JP14703583 A JP 14703583A JP H0510160 B2 JPH0510160 B2 JP H0510160B2
- Authority
- JP
- Japan
- Prior art keywords
- tank
- methane fermentation
- heating
- fermentation
- stirring
- 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 - Lifetime
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Classifications
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M21/00—Bioreactors or fermenters specially adapted for specific uses
- C12M21/04—Bioreactors or fermenters specially adapted for specific uses for producing gas, e.g. biogas
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/02—Biological treatment
- C02F11/04—Anaerobic treatment; Production of methane by such processes
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M27/00—Means for mixing, agitating or circulating fluids in the vessel
- C12M27/02—Stirrer or mobile mixing elements
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M29/00—Means for introduction, extraction or recirculation of materials, e.g. pumps
- C12M29/18—External loop; Means for reintroduction of fermented biomass or liquid percolate
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M41/00—Means for regulation, monitoring, measurement or control, e.g. flow regulation
- C12M41/12—Means for regulation, monitoring, measurement or control, e.g. flow regulation of temperature
- C12M41/18—Heat exchange systems, e.g. heat jackets or outer envelopes
- C12M41/24—Heat exchange systems, e.g. heat jackets or outer envelopes inside the vessel
-
- 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
- Life Sciences & Earth Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Health & Medical Sciences (AREA)
- Organic Chemistry (AREA)
- Zoology (AREA)
- Bioinformatics & Cheminformatics (AREA)
- Wood Science & Technology (AREA)
- Genetics & Genomics (AREA)
- Biochemistry (AREA)
- Biomedical Technology (AREA)
- General Engineering & Computer Science (AREA)
- Sustainable Development (AREA)
- Microbiology (AREA)
- Biotechnology (AREA)
- General Health & Medical Sciences (AREA)
- Molecular Biology (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- General Chemical & Material Sciences (AREA)
- Analytical Chemistry (AREA)
- Thermal Sciences (AREA)
- Physics & Mathematics (AREA)
- Water Supply & Treatment (AREA)
- Environmental & Geological Engineering (AREA)
- Hydrology & Water Resources (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Treatment Of Sludge (AREA)
- Processing Of Solid Wastes (AREA)
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
Description
【発明の詳細な説明】
本発明は、メタン発酵システムの一部を成すメ
タン発酵槽に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a methane fermentor forming part of a methane fermentation system.
最近、ローカルエネルギ創出および環境汚染な
どの公害防止の一環として、農畜産廃棄物による
メタン発酵が大きくクローズアツプされて来てお
り、大小様々なメタン発酵システムについて、そ
の実用化を目指し開発努力が続けられている。現
時の技術水準では、豚10000頭を越えるような大
規模なメタン発酵システムは、下水処理場の汚泥
消化システムに近いものとなり、システム設備費
が嵩む。したがつて、このようなメタン発酵シス
テムを設備可能な需要家は、極めて少ない。他
方、豚500〜5000頭の中小企業規模の場合、中規
模又は小規模なメタン発酵システムを設備可能な
需要家は多い。が、これらの需要家にとつては、
システム設備費として投資可能な資金量が比較的
少なく、しかも、メタン発酵システムの全コスト
に対するメタン発酵槽自体の価格及び施工費の占
める割合が一般に極めて大きいことから、メタン
発酵槽のコストパーフオーマンスがメタン発酵シ
ステム導入可否の鍵を握つている。 Recently, methane fermentation using agricultural and livestock waste has been attracting attention as part of efforts to create local energy and prevent environmental pollution, and efforts are being made to develop methane fermentation systems of various sizes for practical use. It is being With the current state of technology, a large-scale methane fermentation system for over 10,000 pigs would be similar to a sludge digestion system at a sewage treatment plant, which would increase system equipment costs. Therefore, there are very few customers who can install such a methane fermentation system. On the other hand, in the case of small and medium-sized enterprises with 500 to 5,000 pigs, there are many customers who can install medium-scale or small-scale methane fermentation systems. However, for these consumers,
The amount of funds that can be invested in system equipment costs is relatively small, and the price and construction costs of the methane fermentation tank itself generally account for a large proportion of the total cost of the methane fermentation system, so the cost performance of the methane fermentation tank is low. This holds the key to whether or not a methane fermentation system can be introduced.
第1図に、上記中小規模のメタン発酵システム
の一例の全体が示され、このメタン発酵システム
に円筒状縦型のメタン発酵槽が使用されている。 FIG. 1 shows an entire example of the above-mentioned medium-sized and small-scale methane fermentation system, and a cylindrical vertical methane fermentation tank is used in this methane fermentation system.
まず、メタン発酵システムの概略を説明する。
豚舎1から廃棄物溜め2に排出された糞尿3は、
廃棄物汲上げポンプ4により円筒状縦型のメタン
発酵槽5内に汲み上げられる。このメタン発酵槽
5内には、下部で吸込み上部で吐出する型の攪拌
ポンプ6が設けられ、この攪拌ポンプ6から離れ
てメタン発酵槽5の中央に、上下方向に長い加温
用内部温水コイル7が設けられている。攪拌ポン
プ6は電動機により駆動され、メタン発酵槽5内
には電気配線8が通つている。 First, an overview of the methane fermentation system will be explained.
The manure 3 discharged from the pigpen 1 into the waste reservoir 2 is
The waste is pumped into a cylindrical vertical methane fermentation tank 5 by a pump 4 . This methane fermentation tank 5 is provided with a stirring pump 6 that sucks in at the bottom and discharges at the top. 7 is provided. The stirring pump 6 is driven by an electric motor, and an electric wiring 8 runs through the methane fermentation tank 5.
上記メタン発酵槽5で生成された消化メタンガ
スは、脱水装置9及び脱硫装置10を経て水封式
ガスホルダ11に供給される。ガスホルダ11内
に保持されたメタンガスの一部はボイラ12の燃
料として使用され、このボイラ12で生成された
温水は、上記加温用内部温水コイル7へ送給され
る。 Digested methane gas generated in the methane fermentation tank 5 is supplied to a water seal gas holder 11 via a dehydrator 9 and a desulfurizer 10. A part of the methane gas held in the gas holder 11 is used as fuel for the boiler 12, and hot water produced by the boiler 12 is sent to the internal hot water coil 7 for heating.
上述した円筒状縦型メタン発酵槽5には次の様
な欠点が存在する。 The above-mentioned cylindrical vertical methane fermentation tank 5 has the following drawbacks.
1 価格面から、中間断熱材を有する二重繊維強
化プラスチツク板により作られた円筒槽が利用
されるが、この円筒槽は、その内容積が大きく
なるにつれて輸送および加温による発酵効率の
低下を防止するため高さが高くなり、そのため
地震や台風の際倒壊し易い。例えば、豚500頭
に対応する規模のメタン発酵システムにおい
て、メタン発酵槽の内容積は20m3(タンク外側
寸法:φ2280mm×5921mmH)が限界であり、高
さを低くして外径を大きくすると輸送が困難と
なる。1. Due to cost considerations, cylindrical tanks made of double fiber-reinforced plastic plates with intermediate insulation are used; however, as the internal volume of these cylindrical tanks increases, the fermentation efficiency decreases due to transportation and heating. In order to prevent this, the height is increased, which makes it more likely to collapse during an earthquake or typhoon. For example, in a methane fermentation system that can accommodate 500 pigs, the internal volume of the methane fermentation tank is limited to 20m3 (tank outside dimensions: φ2280mm x 5921mmH), and if the height is lowered and the outer diameter is increased, transportation is possible. becomes difficult.
2 高さが高くなると、メタン発酵槽5内の発酵
液の水圧が大きくなり、メタン発酵槽5の底部
の耐水圧が困難となる。2. As the height increases, the water pressure of the fermented liquid in the methane fermentation tank 5 increases, making it difficult to withstand water pressure at the bottom of the methane fermentation tank 5.
3 高さが高くなると、廃棄物汲上げポンプ4及
び攪拌ポンプ6の揚程が大きくなり、規模の割
にはこれらポンプ4及び6の消費エネルギーが
増大してしまう。3. As the height increases, the lift height of the waste pump 4 and stirring pump 6 increases, and the energy consumption of these pumps 4 and 6 increases considering their scale.
4 高さが高くなると避雷針その他の落雷対策が
必要となる。4. Higher heights require lightning rods and other lightning protection measures.
5 加温用内部温水コイル7及び攪拌ポンプ6の
保守が困難である。5. Maintenance of the internal heating coil 7 and stirring pump 6 is difficult.
6 加温用内部温水コイルの発酵効率の低下を来
たす、すなわち発酵効率の低下を防ぐには、タ
ンク内水平方向の加熱を均一にするため温水コ
イルが同心円状多重構造となる。6. In order to prevent a decrease in the fermentation efficiency of the internal hot water coil for heating, that is, to prevent a decrease in fermentation efficiency, the hot water coil has a concentric multilayer structure in order to uniformly heat the tank in the horizontal direction.
第2図に、円筒状横型メタン発酵槽の典型例
が示されている。このメタン発酵槽15は、横
方向に一定間隔を置いて、攪拌ポンプ6と同型
の攪拌ポンプ16を3個有している。これら攪
拌ポンプ16は、メタン発酵槽15のタンク1
5aと一体不可分である。また、タンク15a
の側部からタンク15aの下部においてタンク
15aの横方向に加温用内部温水コイル17が
延設されている。この加温用内部温水コイル1
7もタンク15aと一体不可分である。 FIG. 2 shows a typical example of a cylindrical horizontal methane fermentor. This methane fermentation tank 15 has three stirring pumps 16 of the same type as the stirring pump 6, spaced apart from each other in the lateral direction. These stirring pumps 16 are connected to the tank 1 of the methane fermentation tank 15.
It is inseparable from 5a. In addition, the tank 15a
An internal hot water coil 17 for heating extends in the lateral direction of the tank 15a from the side of the tank 15a to the lower part of the tank 15a. This heating internal hot water coil 1
7 is also inseparable from the tank 15a.
上述した円筒状横型メタン発酵槽15には、
次の様な欠点が存在する。 The above-mentioned cylindrical horizontal methane fermentation tank 15 includes:
There are the following drawbacks.
7 攪拌ポンプ16及び加温用内部温水コイル1
7は、タンク15aと一体不可分であるため保
守点検が困難であり、保守点検を行うとすれば
タンク15a内を空にしなければならない。7 Stirring pump 16 and internal heating coil 1
7 is inseparable from the tank 15a, making maintenance and inspection difficult.If maintenance and inspection are to be performed, the tank 15a must be emptied.
8 メタン発酵槽15は普通型トラツク輸送が出
来かつ内容積を大にするには外径寸法が直径
2.8m以下で長さが10m以下であるが、発酵槽
15の全長に亘る均一な加温と攪拌が困難であ
る。8 The methane fermentation tank 15 can be transported by ordinary truck, and in order to increase the internal volume, the outer diameter must be
Although the length is 2.8 m or less and the length is 10 m or less, uniform heating and stirring over the entire length of the fermenter 15 is difficult.
本発明の目的は、従来の円筒状縦型及び横型の
メタン発酵槽の欠点を除去し、加温及び攪拌効果
を高めてメタン発酵性能を向上せしめるとともに
加温及び攪拌装置の保守点検が容易なメタン発酵
槽を提供することである。この目的を達成するた
めの本発明は、円筒状横型メタン発酵槽を構成す
るタンクの頂部に、該タンクの長手方向に沿つて
一定間隔毎に複数個の挿入口を開口し、この挿入
口に設けられた着脱用フランジに、上端部に前記
着脱用フランジに載置されるスペーサを有して、
このスペーサの下方に延設された複数本の棒材及
び該棒材の下端に固着された底板とから成る支持
枠と、該支持枠に設置された水中型攪拌ポンプ及
びこの攪拌ポンプから液面の上方に延びる吐出管
と、該水中型攪拌ポンプと吐出管の周囲を螺旋状
に取り巻く加温用内部温水コイルとから構成され
た加温・攪拌ユニツトを着脱自在に配設したこと
を特徴とする。 The purpose of the present invention is to eliminate the drawbacks of conventional cylindrical vertical and horizontal methane fermenters, enhance the heating and stirring effects, improve methane fermentation performance, and facilitate maintenance and inspection of the heating and stirring equipment. An object of the present invention is to provide a methane fermentation tank. In order to achieve this object, the present invention has a plurality of insertion ports opened at regular intervals along the longitudinal direction of the tank at the top of a tank constituting a cylindrical horizontal methane fermentation tank. The provided attachment/detachment flange has a spacer placed on the attachment/detachment flange at its upper end,
A support frame consisting of a plurality of rods extending below the spacer and a bottom plate fixed to the lower end of the rods, a submersible stirring pump installed in the support frame, and a liquid level from the stirring pump to the support frame. A heating/stirring unit consisting of a discharge pipe extending upward, and an internal hot water coil for heating spirally surrounding the submersible stirring pump and the discharge pipe is detachably installed. do.
以下、第3図ないし第5図に基づいて、本発明
の好適な実施例を詳細に説明する。ほぼ横型円筒
状のメタン発酵槽のタンク20は、複数本の脚部
21により基礎面22に固定されている。タンク
20の全壁は、繊維強化プラスチツクから成る内
壁及び外壁を有し、これらの壁間にポリウレタン
から成る断熱材を充填した構造を有する。タンク
20の外径および全長は、メタン発酵システムの
規模に応じて適当に選定されている。 Hereinafter, preferred embodiments of the present invention will be described in detail based on FIGS. 3 to 5. A substantially horizontal cylindrical methane fermentation tank 20 is fixed to a base surface 22 by a plurality of legs 21. The entire wall of the tank 20 has an inner wall and an outer wall made of fiber-reinforced plastic, and has a structure in which a heat insulating material made of polyurethane is filled between these walls. The outer diameter and overall length of the tank 20 are appropriately selected depending on the scale of the methane fermentation system.
しかし大型トレラーなど特殊運搬車でなく低床
の大型トラツク輸送を考慮すると外径2.8m以下
が好ましい。 However, considering transportation by large low-floor trucks rather than special transport vehicles such as large trailers, an outer diameter of 2.8 m or less is preferable.
内容積最大50m3のものをユニツト化し規模の拡
大に応じて増設することが容易である。 It is easy to make units with a maximum internal volume of 50m3 and expand them as the scale expands.
上記タンク20の頂部には、このタンク20の
長手方向に一定間隔を置いて複数個の挿入口23
が若干上方に突出して設けられている。各挿入口
23は、その横断面が正方形であり、上端に角形
の着脱用フランジ24を有する。 A plurality of insertion ports 23 are provided at the top of the tank 20 at regular intervals in the longitudinal direction of the tank 20.
is provided so as to protrude slightly upward. Each insertion port 23 has a square cross section and has a rectangular attachment/detachment flange 24 at its upper end.
各挿入口23からタンク20内に加温・攪拌ユ
ニツト25が挿入されている。この加温・攪拌ユ
ニツト25は、主として、上下に延設された複数
本の棒材26とこれら棒材26の下端に固着され
た1枚の底板27とから成る支持枠28と、この
支持枠28の軸心部に設置された、攪拌器として
の水中型攪拌ポンプ29と、この攪拌ポンプ29
から支持枠28内を上方に延びた吐出管30と、
攪拌ポンプ29及び吐出管30を螺旋状に取巻
き、棒材26に内接しつつ上方に延びた加温用内
部温水コイル31と、挿入口23の着脱用フラン
ジ24に載置される角形スペーサ32とから成
る。 A heating/stirring unit 25 is inserted into the tank 20 from each insertion port 23. This heating/stirring unit 25 mainly consists of a support frame 28 consisting of a plurality of vertically extending rods 26 and a bottom plate 27 fixed to the lower ends of these rods 26, and this support frame. A submersible stirring pump 29 as an agitator installed at the axial center of the stirring pump 28 , and this stirring pump 29
a discharge pipe 30 extending upwardly within the support frame 28;
An internal hot water coil 31 for heating spirally surrounds the stirring pump 29 and the discharge pipe 30 and extends upward while being inscribed in the bar 26; and a square spacer 32 placed on the attachment/detachment flange 24 of the insertion port 23. Consists of.
上記支持枠28の底板27には、攪拌ポンプ2
9が設けてあり、攪拌ポンプ29の下端部に攪拌
ポンプ29を介して吐出管30に連通した発酵液
循環用吸入口33が配設されている。 A stirring pump 2 is provided on the bottom plate 27 of the support frame 28.
9 is provided, and a suction port 33 for fermentation liquid circulation is provided at the lower end of the stirring pump 29 and communicated with the discharge pipe 30 via the stirring pump 29.
上記吐出管30の上端には、第4図及び第5図
に示すように、十字状にクロスし、かつ、それぞ
れ4個の端部で開口した吐出管口34が設けられ
ている。また、この吐出管34は、発酵液35の
液面よりも上方で開口し、しかも、循環効率向上
のため加温器としての加温用内部温水コイル31
の内側で3個が開口し、外側で1個が開口してい
る。 At the upper end of the discharge pipe 30, as shown in FIGS. 4 and 5, discharge pipe ports 34 are provided which cross in a cross shape and are open at each of four ends. Further, this discharge pipe 34 opens above the liquid level of the fermentation liquid 35, and furthermore, in order to improve circulation efficiency, an internal hot water coil 31 for heating is used as a heater.
Three are open on the inside and one is open on the outside.
上記スペーサ32は、タンク20の壁と同一構
造の壁を有し、中空であつて、第5図に示すよう
に、対向した2面にそれぞれケーブル接続用端子
箱36と温水入管口37及び温水出管口38とを
有し、他の対向した2面にそれぞれガス放出管口
39を有する。これらガス放出管口39は、メタ
ン発酵システムの他の部分を構成するガス精製貯
溜装置へ接続されている。上記ケーブル接続用端
子箱36から攪拌ポンプ29中の図示しないモー
タへ電気ケーブル40が延設されている。上記温
水入管口37及び温水出管口38は、加温用内部
温水コイル31に接続されている。 The spacer 32 has a wall with the same structure as the wall of the tank 20, is hollow, and has a terminal box 36 for cable connection, a hot water inlet pipe 37, and a hot water inlet port 37 on two opposing sides, respectively, as shown in FIG. It has an outlet pipe port 38, and has gas discharge pipe ports 39 on the other two opposing sides. These gas discharge ports 39 are connected to a gas purification and storage device that constitutes the other part of the methane fermentation system. An electric cable 40 extends from the cable connection terminal box 36 to a motor (not shown) in the stirring pump 29. The hot water inlet port 37 and the hot water outlet port 38 are connected to the internal hot water coil 31 for heating.
上記スペーサ32の上面には、正方形の上蓋4
1が載置されている。上蓋41のほゞ中央にバル
ブ41aを装着した発酵ガス検査管41bがタン
ク20内と大気側を連通するように配設されてい
る。この発酵ガス検査管41bは、タンク20内
でメタン発酵が正常に行われるまでの間に、タン
ク20内のガスをサンプリングするためのもので
ある。 A square top lid 4 is provided on the top surface of the spacer 32.
1 is placed. A fermentation gas inspection tube 41b equipped with a valve 41a is disposed approximately in the center of the upper lid 41 so as to communicate between the inside of the tank 20 and the atmosphere side. This fermentation gas test tube 41b is for sampling the gas in the tank 20 until methane fermentation is normally performed in the tank 20.
上記加温・攪拌ユニツト25は、タンク20の
内容積の大小及び必要加温・攪拌能力によつて1
個又は複数個設けられる。 The number of heating/stirring units 25 may vary depending on the internal volume of the tank 20 and the required heating/stirring capacity.
One or more can be provided.
上記タンク20の一の側面(第4図中、左側
面)には、上部に発酵原液投入管口42が設けら
れ、下部にドレン43が設けられている。 One side (left side in FIG. 4) of the tank 20 is provided with a fermentation stock solution input pipe port 42 at the top and a drain 43 at the bottom.
上記タンク20の他の側面(第4図中、右側
面)には、上部に発酵廃液排出管口44及び液面
計45が設けられ、下部にドレン43が設けられ
ている。 On the other side of the tank 20 (the right side in FIG. 4), a fermentation waste liquid discharge pipe port 44 and a liquid level gauge 45 are provided at the top, and a drain 43 is provided at the bottom.
以下、上述した本発明のメタン発酵槽の作用を
説明する。発酵原液が外部に存在する第1図に示
すような吸上ポンプ4により発酵原液投入管口4
2を経てタンク20内に投入され、発酵原液の特
性に応じた滞留日数を経て、その間に発酵し、発
酵廃液として発酵廃液排出管口44からオーバー
フローする。すなわち、メタン発酵槽の全体を静
態的に観れば、毎日発酵原液が投入される毎にそ
の液量に応じて発酵廃液が排出され、タンク20
内の液面は一定に規制されている。 Hereinafter, the operation of the methane fermentation tank of the present invention described above will be explained. Fermentation stock solution is introduced into the fermentation stock solution input pipe port 4 by a suction pump 4 as shown in FIG.
2, it is put into the tank 20, and fermented during the retention period depending on the characteristics of the fermentation liquid, and overflows from the fermentation waste liquid discharge pipe port 44 as fermentation waste liquid. In other words, if we look at the entire methane fermentation tank statically, each time the fermentation stock solution is added every day, the fermentation waste solution is discharged according to the amount of the fermentation stock solution, and the fermentation waste solution is discharged from the tank 20.
The liquid level inside is regulated to a constant level.
発酵原液は、加温・攪拌ユニツト25により十
分な攪拌と加温とを受けて、嫌気性環境内でタン
ク20内の発酵液35に内在するメタン菌による
メタン発酵が促進され、発酵液35の上部空間に
メタンガスを放出しつつ、発酵原液投入管口42
側から発酵廃液排出管口44側へ徐々に流動して
行く。 The fermentation stock solution is sufficiently stirred and heated by the heating/stirring unit 25 to promote methane fermentation by methane bacteria present in the fermentation solution 35 in the tank 20 in an anaerobic environment. While releasing methane gas into the upper space, the fermentation stock solution input pipe port 42
The fermentation waste liquid gradually flows from the side to the fermentation waste liquid discharge pipe port 44 side.
発酵液35の上部空間に放出されたメタンガス
は、ガス放出管口39を経てガス精製貯溜装置の
方へ送られる。 The methane gas released into the upper space of the fermentation liquid 35 is sent to the gas purification and storage device via the gas release pipe port 39.
上記メタン発酵槽内においては、発酵液循環用
吸水口33から発酵液35が攪拌ポンプ29によ
り汲み上げられ、吐出管口34より加温用内部温
水コイル31の内外に散布される。散布された発
酵液は、加温用内部温水コイル31の内側又は外
側を通過しつつ加温され、再び発酵液循環用吸入
口33の方へ下降して行く。このようにして効率
的に攪拌と加温とが繰り返される。 In the methane fermentation tank, the fermentation liquid 35 is pumped up by the stirring pump 29 from the water intake port 33 for fermentation liquid circulation, and is sprayed inside and outside of the internal hot water coil 31 for heating from the discharge pipe port 34 . The sprayed fermentation liquid is heated while passing inside or outside the heating internal hot water coil 31, and descends again toward the fermentation liquid circulation suction port 33. In this way, stirring and heating are efficiently repeated.
上記加温・攪拌ユニツト25は、そのスペーサ
32の部分において、着脱用フランジ24に着脱
自在に支持されているのみであるから、タンク2
0から簡単に取外すことができ、また取外してい
る間は、上蓋41を着脱用フランジ24に密封状
態で取付け、それによつてタンク20内の嫌気性
環境を損うことがない。 Since the heating/stirring unit 25 is only detachably supported by the attaching/detachable flange 24 at the spacer 32, the tank 2
The upper cover 41 can be easily removed from the tank 20, and during removal, the upper cover 41 is attached to the attachment/detachment flange 24 in a sealed state, thereby not damaging the anaerobic environment inside the tank 20.
上述の通り、本発明は円筒状横型のタンクの頂
部に着脱フランジ付挿入口を設ける一方、支持枠
内において加温器及び攪拌器が配設され、支持枠
の上部にスペーサを有する加温・攪拌ユニツト
が、上記挿入口からタンク内に挿入され、スペー
サが着脱用フランジに取外し自在に取付けられる
ようにしたので、タンクの容積、発酵液の特性、
及び寒冷地又は温暖地などの気象条件などの種々
の条件に応じて加温・攪拌ユニツトの数を自由に
選定できる。 As mentioned above, the present invention provides a heating/discharging system in which an insertion port with a removable flange is provided at the top of a cylindrical horizontal tank, a warmer and an agitator are provided within a support frame, and a spacer is provided at the top of the support frame. The stirring unit is inserted into the tank from the insertion port, and the spacer is removably attached to the detachable flange, so the volume of the tank, the characteristics of the fermented liquid,
The number of heating/stirring units can be freely selected depending on various conditions such as weather conditions in cold regions or warm regions.
本発明にかかるメタン発酵槽は、基本的な形状
として円筒状横型を採用しており、必然的に全高
は一定値以下に制限される。それに伴つて地震と
か台風で倒壊する惧れがなく、且つ槽内の発酵液
の水圧が必要以上に大きくなることが防止され、
メタン発酵槽を構成する材料に特別な耐圧性が要
求されないという効果がある。更に廃棄物汲上げ
ポンプとか攪拌ポンプの揚程が小さく、これらポ
ンプの駆動に要する消費エネルギーは小さくて済
むという効果が得られる。 The methane fermentation tank according to the present invention adopts a horizontal cylindrical shape as its basic shape, and the total height is necessarily limited to a certain value or less. Along with this, there is no risk of it collapsing due to an earthquake or typhoon, and the water pressure of the fermentation liquid in the tank is prevented from increasing more than necessary.
This has the advantage that the materials constituting the methane fermentation tank do not require special pressure resistance. Furthermore, the waste lifting pump and stirring pump have a small lift, and the energy consumption required to drive these pumps can be reduced.
更に発酵液が攪拌ポンプによつて汲上げられ、
加温用内部温水コイルの内側及び外側を通過しつ
つ加温されることにより、発酵液の循環速度が高
められるとともに、攪拌条件と加温条件を相互に
関連付けてコントロールできて、メタン発酵作用
が促進されるという効果を発揮する。 Furthermore, the fermentation liquid is pumped up by a stirring pump,
By being heated while passing through the inside and outside of the internal heating coil, the circulation speed of the fermentation liquid is increased, and the stirring conditions and heating conditions can be controlled in relation to each other, thereby reducing the methane fermentation effect. It has the effect of being promoted.
また、加温・攪拌ユニツトは、タンクに対し取
付・取外し自在であるからメタン発酵槽の保守点
検が容易であり、しかも部品の交換等のメンテナ
ンスも簡単に行えるという効果が得れる。 Furthermore, since the heating/stirring unit can be attached to and removed from the tank, maintenance and inspection of the methane fermentation tank is easy, and maintenance such as replacement of parts can also be easily performed.
第1図は、従来技術にかかる一のメタン発酵シ
ステムの概略説明図、第2図は、従来技術にかか
る横型円筒のメタン発酵槽の概略縦断面図、第3
図は、本発明にかかるメタン発酵槽の一部省略平
面図、第4図は、第3図における−線断面
図、第5図は第4図における−線断面図であ
る。
20……タンク、23……挿入口、24……着
脱用フランジ、25……加温・攪拌ユニツト、2
8……支持枠、29……攪拌器、31……加温
器、32……スペーサ。
FIG. 1 is a schematic explanatory diagram of a methane fermentation system according to the prior art, FIG. 2 is a schematic vertical sectional view of a horizontal cylindrical methane fermentation tank according to the prior art, and FIG.
4 is a partially omitted plan view of the methane fermentation tank according to the present invention, FIG. 4 is a cross-sectional view taken along the line -- in FIG. 3, and FIG. 5 is a cross-sectional view taken along the line -- in FIG. 4. 20...Tank, 23...Insertion port, 24...Detachable flange, 25...Heating/stirring unit, 2
8... Support frame, 29... Stirrer, 31... Warmer, 32... Spacer.
Claims (1)
頂部に、該タンクの長手方向に沿つて一定間隔毎
に複数個の挿入口を開口し、この挿入口に設けら
れた着脱用フランジに、上端部に前記着脱用フラ
ンジに載置されるスペーサを有して、このスペー
サの下方に延設された複数本の棒材及び該棒材の
下端に固着された底板とから成る支持枠と、該支
持枠に設置された水中型攪拌ポンプ及びこの攪拌
ポンプから液面の上方に延びる吐出管と、該水中
型攪拌ポンプと吐出管の周囲を螺旋状に取り巻く
加温用内部温水コイルとから構成された加温・攪
拌ユニツトを着脱自在に配設したことを特徴とす
るメタン発酵槽。1 A plurality of insertion ports are opened at regular intervals along the longitudinal direction of the tank at the top of the tank constituting the cylindrical horizontal methane fermentation tank, and the upper end is inserted into the attachment/detachment flange provided in the insertion port. a support frame comprising a spacer placed on the attachment/detachment flange, a plurality of rods extending below the spacer, and a bottom plate fixed to the lower end of the rod; It consists of a submersible stirring pump installed in a frame, a discharge pipe extending from the stirring pump above the liquid level, and an internal hot water coil for heating that spirally surrounds the submersible stirring pump and the discharge pipe. A methane fermentation tank characterized by a removable heating/stirring unit.
Priority Applications (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP58147035A JPS6038093A (en) | 1983-08-10 | 1983-08-10 | Methane fermentation tank |
| GB08419807A GB2144767B (en) | 1983-08-10 | 1984-08-03 | Methane fermenter |
| KR1019840004764A KR920001261B1 (en) | 1983-08-10 | 1984-08-09 | Methane fermenter |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP58147035A JPS6038093A (en) | 1983-08-10 | 1983-08-10 | Methane fermentation tank |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6038093A JPS6038093A (en) | 1985-02-27 |
| JPH0510160B2 true JPH0510160B2 (en) | 1993-02-08 |
Family
ID=15421049
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP58147035A Granted JPS6038093A (en) | 1983-08-10 | 1983-08-10 | Methane fermentation tank |
Country Status (3)
| Country | Link |
|---|---|
| JP (1) | JPS6038093A (en) |
| KR (1) | KR920001261B1 (en) |
| GB (1) | GB2144767B (en) |
Families Citing this family (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2508855B2 (en) * | 1989-09-08 | 1996-06-19 | 井関農機株式会社 | House environment control device in facility gardening |
| JP2508856B2 (en) * | 1989-09-08 | 1996-06-19 | 井関農機株式会社 | Complex environmental control system for facility gardening |
| SE505749C2 (en) * | 1995-08-10 | 1997-10-06 | Va Teknik & Vattenvaard I Broe | Methods and apparatus for sludge digestion |
| JP4631043B2 (en) * | 2003-09-04 | 2011-02-16 | 国立大学法人 筑波大学 | Methane generation method and two-phase methane generator used therefor |
| JP4577719B2 (en) * | 2005-04-28 | 2010-11-10 | 荏原エンジニアリングサービス株式会社 | Methane fermentation method and apparatus using horizontal multi-stage methane fermenter |
| ITMI20070116A1 (en) | 2007-01-26 | 2008-07-27 | Agroittica Spa | PROCEDURE AND PLANT FOR THE PRODUCTION OF ENERGY AND MATERIAL COMPOSED BY AGRICULTURAL WASTE CONTAINING CELLULOSE |
| CH710436B1 (en) | 2007-09-04 | 2016-06-15 | Hitachi Zosen Inova Ag | Reclining tubular fermenter with a means for heating. |
| GB201014693D0 (en) * | 2010-09-06 | 2010-10-20 | Ch4E Ltd | Digester |
| WO2014072577A1 (en) * | 2012-11-07 | 2014-05-15 | Maa- Ja Elintarviketalouden Tutkimuskeskus | Bioreactor apparatus |
| CH708197A1 (en) * | 2013-06-10 | 2014-12-15 | Axpo Kompogas Engineering Ag | Construction method of a fermenter for a biogas plant. |
| CN112725171A (en) * | 2021-02-03 | 2021-04-30 | 邵阳学院 | Yeast fermenting device with stirring structure and capable of heating |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB911164A (en) * | 1960-01-13 | 1962-11-21 | Roger Graham Knibb | Means for heating and circulating sludge in a sludge digester tank |
| JPS4330542Y1 (en) * | 1964-01-21 | 1968-12-12 | ||
| GB1451398A (en) * | 1974-05-24 | 1976-09-29 | Biomechanics Ltd | Anaerobic digestion plants and methods of operating the same |
| NL8001959A (en) * | 1979-10-30 | 1981-06-01 | Pacques Bv | CLOSED DEVICE FOR PREPARING BIOGAS FROM MANURE. |
-
1983
- 1983-08-10 JP JP58147035A patent/JPS6038093A/en active Granted
-
1984
- 1984-08-03 GB GB08419807A patent/GB2144767B/en not_active Expired
- 1984-08-09 KR KR1019840004764A patent/KR920001261B1/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| GB2144767B (en) | 1987-07-15 |
| KR920001261B1 (en) | 1992-02-08 |
| JPS6038093A (en) | 1985-02-27 |
| KR850001895A (en) | 1985-04-10 |
| GB8419807D0 (en) | 1984-09-05 |
| GB2144767A (en) | 1985-03-13 |
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