JPH0243519Y2 - - Google Patents

Info

Publication number
JPH0243519Y2
JPH0243519Y2 JP7193784U JP7193784U JPH0243519Y2 JP H0243519 Y2 JPH0243519 Y2 JP H0243519Y2 JP 7193784 U JP7193784 U JP 7193784U JP 7193784 U JP7193784 U JP 7193784U JP H0243519 Y2 JPH0243519 Y2 JP H0243519Y2
Authority
JP
Japan
Prior art keywords
tank
hot water
gas
storage tank
water storage
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
JP7193784U
Other languages
Japanese (ja)
Other versions
JPS60186100U (en
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 filed Critical
Priority to JP1984071937U priority Critical patent/JPS60186100U/en
Publication of JPS60186100U publication Critical patent/JPS60186100U/en
Application granted granted Critical
Publication of JPH0243519Y2 publication Critical patent/JPH0243519Y2/ja
Granted legal-status Critical Current

Links

Classifications

    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/30Fuel from waste, e.g. synthetic alcohol or diesel

Landscapes

  • Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
  • Treatment Of Sludge (AREA)

Description

【考案の詳細な説明】 この考案はガスを貯留する貯槽に関するもので
特に寒冷地で農畜産及び水産廃棄物を利用し、中
小規模のメタン発酵を行ない、発生するガスを貯
留するのに適したガスホルダーを提供するもので
ある。
[Detailed explanation of the invention] This invention relates to a storage tank for storing gas, and is particularly suitable for storing the gas generated by performing small- to medium-scale methane fermentation using agricultural, livestock, and fishery waste in cold regions. It provides a gas holder.

従来、農畜産廃棄物は肥料として利用されて来
たが、近年エネルギーの有効利用を目的とし、微
生物によりメタン発酵を行なわせガス化して使用
する方法が中小規模のスケールで研究実施されて
いる。
Traditionally, agricultural and livestock waste has been used as fertilizer, but in recent years, with the aim of effectively utilizing energy, research has been conducted on small and medium-sized scales to use microorganisms to perform methane fermentation and gasify the waste.

しかしながらメタン発酵は35〜40℃の高温で発
酵を行ない、得られたガスを1時貯留し必要な時
に取り出して燃料に供するため温暖地においては
問題はないが寒冷地においては発酵生成したガス
に多量に含まれる水分が凍結し配管を閉鎖すると
か、ガスの貯留に浮屋根式のガスホルダーを使用
すると水封に使用したシール水が凍結して浮屋根
の昇降機能が失なわれるので水封には不凍液を使
用しなければならないので装置が高価になる等の
不便があつた。そこで考案者らは寒冷地において
も温暖地におけると同様、メタン発酵を行なわ
せ、発生したガスを何のトラブルもなく貯留でき
るガスホルダーを得んと研究を進めた結果、メタ
ン発酵で発生したガスを浮屋根式のガスホルダー
で貯留する場合にガスホルダーの浮屋根の内外に
外槽と内槽を設け、内槽と外槽の間にシール水を
入れてその中に浮屋根の側壁部を挿入して水封
し、前記内槽の内部には温水貯槽を設けてシール
水の凍結を防止すると共に貯留ガスを加温し水分
の凍結を防止することによつて解決したものであ
る。
However, methane fermentation is carried out at a high temperature of 35 to 40 degrees Celsius, and the resulting gas is stored for a period of time and taken out when needed to serve as fuel, so there is no problem in warm regions, but in cold regions, the gas produced by fermentation is A large amount of moisture may freeze and close the piping, or if a floating roof type gas holder is used to store gas, the seal water used for the water seal will freeze and the floating roof will lose its ability to rise and fall. Since antifreeze must be used in this method, there are inconveniences such as the equipment being expensive. Therefore, the inventors carried out research to create a gas holder that could allow methane fermentation to occur in cold regions as well as in warm regions, and store the generated gas without any trouble. When storing gas in a floating roof type gas holder, an outer tank and an inner tank are installed inside and outside the floating roof of the gas holder, and seal water is placed between the inner tank and the outer tank, and the side wall of the floating roof is placed inside the tank. This problem was solved by inserting the inner tank and sealing it with water, and providing a hot water storage tank inside the inner tank to prevent the seal water from freezing and warming the stored gas to prevent the water from freezing.

この考案の例を添付の図面により説明すると、
1は外槽でその内壁2、底面3及び天井4の外側
にはグラスウールその他の断熱材5の層を設け断
熱効果を良好にすると共に天井4の上部には空気
抜き管6を設け外槽1内外の空気を連通させてあ
る。又底面3の面上に内槽7を同心状に固定して
密封し外槽1の側壁2と内槽7の間にはシール水
8を入れ、該シール水8の中に筒状の浮屋根9の
側壁10を挿入し、該側壁10と前記内壁2の間
には転りコロ11,11を設けて浮屋根9の上下
移動を可能にしている。更に前記内槽7の内部で
あつて底面3上には密封した温水貯槽12を同心
状に固定している。そして浮屋根9の内側にはガ
ス流入用配管13、及びガス流出用配管14を設
け、それぞれ内槽7を貫通して立上らせてある。
又、温水貯槽12の下部には温水循環配管17,
17′、及び18,18′を設け、上部には空気抜
き管19を設けてある。又内槽7には空気抜き管
16を設ける。
An example of this invention will be explained with reference to the attached drawings.
Reference numeral 1 denotes an outer tank, and a layer of glass wool or other heat insulating material 5 is provided on the outside of the inner wall 2, bottom surface 3, and ceiling 4 to improve the heat insulation effect, and an air vent pipe 6 is provided at the top of the ceiling 4 to connect the inside and outside of the outer tank 1. The air is communicated with each other. In addition, the inner tank 7 is fixed concentrically on the surface of the bottom 3 and sealed, and seal water 8 is placed between the side wall 2 of the outer tank 1 and the inner tank 7, and a cylindrical floating tube is placed in the seal water 8. A side wall 10 of the roof 9 is inserted, and rolling rollers 11, 11 are provided between the side wall 10 and the inner wall 2 to enable the floating roof 9 to move up and down. Furthermore, a sealed hot water storage tank 12 is fixed concentrically inside the inner tank 7 and on the bottom surface 3. Inside the floating roof 9, a gas inflow pipe 13 and a gas outflow pipe 14 are provided, each penetrating the inner tank 7 and standing upright.
Further, at the bottom of the hot water storage tank 12, there is a hot water circulation pipe 17,
17', and 18, 18', and an air vent pipe 19 is provided at the upper part. Furthermore, an air vent pipe 16 is provided in the inner tank 7.

この考案の装置の運転例を第2図を参照して説
明すると、メタン発酵槽20に人畜の排泄物、発
酵性農産廃棄物等を入れ嫌気状態とし35〜37℃に
加熱して発酵さす。発酵槽20内で発生したメタ
ンを主とするガスは頂部に設けたガス配管13よ
り浮屋根9と内槽7との間のガス溜部21に流入
し、浮屋根9を押し上げる。ガス溜部21のガス
はガス流出用配管14によつて取り出され大部は
ガスボイラー22に供給して該ボイラー22内の
水を加温する。加熱された温水は温水循環配管1
7を流出し、ポンプ23により前記温水貯槽12
内に流入する。温水貯槽12内で温度が下つた温
水は温水循環配管17′を介してボイラー22に
戻し、再び加温して循環させ、この考案の装置が
畜舎等の施設における温水利用であるときには、
温水貯槽12内の水温が常時60〜90℃を維持する
ように加温する。この温水は更に温水貯槽12と
発酵槽20内に設けた加温器24との間を接続す
る循環配管18でポンプ25を介して引き出し該
配管18の途中に設けたスタチツクミキサーの如
き調温器26で冷水と混合し、発酵槽20内の温
度が35〜37℃に保持される如く加温し、冷却した
水は循環配管18′を介して温水貯槽12に戻す。
又、循環配管18で引き出した温水は分岐配管2
7で取出し、畜舎等の暖房、清掃その他の用に供
する。尚、温水を外部に引出して利用するため水
量が減少するが、このため前記循環配管17′に
配管28を接続し、減少分に見合う冷水や前記暖
房の戻り水を補給する。
An example of the operation of the device of this invention will be described with reference to FIG. 2. Human and animal excrement, fermentable agricultural waste, etc. are placed in a methane fermentation tank 20, brought to an anaerobic state, and heated to 35 to 37° C. for fermentation. Gas mainly composed of methane generated in the fermenter 20 flows into a gas reservoir 21 between the floating roof 9 and the inner tank 7 through a gas pipe 13 provided at the top, and pushes up the floating roof 9. The gas in the gas reservoir 21 is taken out through the gas outlet pipe 14, and most of it is supplied to the gas boiler 22 to heat the water in the boiler 22. The heated hot water goes through hot water circulation piping 1
7 is discharged and pumped into the hot water storage tank 12 by the pump 23.
flow inside. The hot water whose temperature has decreased in the hot water storage tank 12 is returned to the boiler 22 via the hot water circulation pipe 17', where it is heated again and circulated.
The water temperature in the hot water storage tank 12 is heated so that it is always maintained at 60 to 90°C. This hot water is further drawn out through a pump 25 through a circulation pipe 18 that connects the hot water storage tank 12 and a heater 24 provided in the fermenter 20, and the temperature is controlled by a static mixer installed in the middle of the pipe 18. The fermenter 20 is mixed with cold water in the vessel 26, heated so that the temperature inside the fermenter 20 is maintained at 35-37°C, and the cooled water is returned to the hot water storage tank 12 via the circulation pipe 18'.
In addition, the hot water drawn out through the circulation pipe 18 is transferred to the branch pipe 2.
It is taken out at step 7 and used for heating, cleaning, etc. of livestock barns, etc. Incidentally, since the hot water is drawn outside for use, the amount of water decreases, but for this reason, a pipe 28 is connected to the circulation pipe 17', and cold water or return water from the heating system is replenished to compensate for the decrease.

一方温水貯槽12を内槽7内に設け、比熱の大
きな温水を保温熱源として貯蔵することにより、
ガスホルダー全体の単位容積当たりの保有熱量が
大きくなるから、外気が急冷されても温度低下は
少なく、更に温水貯槽12は内槽7内の加温され
た空気と接するので放熱が少なくてすみ、その上
シール水8は前記加温された内槽7の側壁10と
接しているから、氷点以下の外気温にあつても氷
結することはなく浮屋根の上下動を円滑にし、ガ
ス溜部21のガスも加温されているので水分が凍
結し配管を詰らせることもない。本考案の装置は
温水槽を独立して設けないので敷地面積が少なく
て済み作業性を良好にし熱経済の改善に役立つ。
On the other hand, by providing a hot water storage tank 12 in the inner tank 7 and storing hot water with a large specific heat as a heat source,
Since the amount of heat retained per unit volume of the entire gas holder is increased, there is little temperature drop even if the outside air is rapidly cooled, and furthermore, since the hot water storage tank 12 is in contact with the heated air in the inner tank 7, less heat radiation is required. Moreover, since the seal water 8 is in contact with the side wall 10 of the heated inner tank 7, it does not freeze even in the outside temperature below the freezing point, and the vertical movement of the floating roof is smooth. Since the gas is also heated, water will not freeze and clog the pipes. Since the device of the present invention does not have a separate hot water tank, it requires less site space, improves workability, and helps improve thermal economy.

上記の如くこの考案の装置は構造が簡単で多く
の利益をもたらすもので特に寒冷地における、中
小規模の農畜産、水産加工時の廃棄物のメタン発
酵時のガスホルダーとして使用しきわめて有益で
ある。
As mentioned above, the device of this invention has a simple structure and brings many benefits, and is extremely useful especially in cold regions when used as a gas holder for methane fermentation of waste from small and medium-scale agriculture and livestock processing and fishery processing. .

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

第1図はこの考案のガスホルダーの側断面図を
示し、第2図はこの考案のガスホルダーの使用例
を示す説明図である。 1……外槽、7……内槽、9……浮屋根、12
……温水貯槽、13……ガス流入用配管、14…
…ガス流出用配管、20……メタン発酵槽、22
……ガスボイラー。
FIG. 1 shows a side sectional view of the gas holder of this invention, and FIG. 2 is an explanatory view showing an example of use of the gas holder of this invention. 1...Outer tank, 7...Inner tank, 9...Floating roof, 12
...Hot water storage tank, 13...Gas inflow piping, 14...
...Gas outflow piping, 20...Methane fermentation tank, 22
...Gas boiler.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] メタン発酵で発生するガスを貯留する浮屋根式
ガスホルダーにおいて、浮屋根の内外にそれぞれ
内槽と外槽を設け、内・外両槽間を水封し、内槽
の内部に温水貯槽を設けて四槽構造となし、温水
貯槽とガスボイラーとの間および温水貯槽と発酵
槽内加温器との間にそれぞれ温水循環配管を配し
たことを特徴とするメタン発酵用ガスホルダー。
In a floating roof type gas holder that stores gas generated from methane fermentation, an inner tank and an outer tank are installed inside and outside the floating roof, a water seal is placed between the inner and outer tanks, and a hot water storage tank is installed inside the inner tank. A gas holder for methane fermentation, characterized in that the gas holder has a four-tank structure, and hot water circulation piping is arranged between the hot water storage tank and the gas boiler, and between the hot water storage tank and the fermentation tank internal heater.
JP1984071937U 1984-05-18 1984-05-18 Gas holder for methane fermentation Granted JPS60186100U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1984071937U JPS60186100U (en) 1984-05-18 1984-05-18 Gas holder for methane fermentation

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1984071937U JPS60186100U (en) 1984-05-18 1984-05-18 Gas holder for methane fermentation

Publications (2)

Publication Number Publication Date
JPS60186100U JPS60186100U (en) 1985-12-10
JPH0243519Y2 true JPH0243519Y2 (en) 1990-11-19

Family

ID=30609879

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1984071937U Granted JPS60186100U (en) 1984-05-18 1984-05-18 Gas holder for methane fermentation

Country Status (1)

Country Link
JP (1) JPS60186100U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105152319A (en) * 2015-07-07 2015-12-16 扬州市正源市政环保工程有限公司 Anaerobic fermentation tower negative pressure protection apparatus

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5745396A (en) * 1980-08-29 1982-03-15 Hoxan Corp Generating device for methane

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5745396A (en) * 1980-08-29 1982-03-15 Hoxan Corp Generating device for methane

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105152319A (en) * 2015-07-07 2015-12-16 扬州市正源市政环保工程有限公司 Anaerobic fermentation tower negative pressure protection apparatus
CN105152319B (en) * 2015-07-07 2017-12-19 扬州市正源市政环保工程有限公司 A kind of anaerobic fermentation tower negative-pressure protection device

Also Published As

Publication number Publication date
JPS60186100U (en) 1985-12-10

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