JPS62800Y2 - - Google Patents

Info

Publication number
JPS62800Y2
JPS62800Y2 JP1981142696U JP14269681U JPS62800Y2 JP S62800 Y2 JPS62800 Y2 JP S62800Y2 JP 1981142696 U JP1981142696 U JP 1981142696U JP 14269681 U JP14269681 U JP 14269681U JP S62800 Y2 JPS62800 Y2 JP S62800Y2
Authority
JP
Japan
Prior art keywords
draft tube
sludge
pipe
tank
steam
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
JP1981142696U
Other languages
Japanese (ja)
Other versions
JPS5848400U (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 JP1981142696U priority Critical patent/JPS5848400U/en
Publication of JPS5848400U publication Critical patent/JPS5848400U/en
Application granted granted Critical
Publication of JPS62800Y2 publication Critical patent/JPS62800Y2/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、消化槽の改良に関するものであ
る。
[Detailed description of the invention] This invention relates to the improvement of a digestion tank.

大型消化槽では一般に、蒸気吹込式の加温手段
と、汚泥のガス撹拌手段とを備えて消火の促進を
図るようにしている。しかし、従来のこの種消化
槽においては、蒸気吹込管と撹拌ガス吹込管及び
汚泥投入管とがそれぞれ他のものとは関連をもた
ずに独立して設けられており、そのため、投入さ
れ冷えた汚泥によつて槽内温度が不均一化して熱
効率が低下したり、蒸気が消化中に含まれる汚泥
を直接加温することにより、その熱によつて微生
物の死滅が生じたりして、消化効率上不十分な点
が多いという問題がある。
Large-scale digestion tanks are generally equipped with steam-injection type heating means and sludge gas agitation means to facilitate extinguishing fires. However, in conventional digesters of this type, the steam blowing pipe, the stirring gas blowing pipe, and the sludge feeding pipe are each installed independently without any connection with the others, and therefore, the steam blowing pipe, the stirring gas blowing pipe, and the sludge feeding pipe are installed independently, so that they are fed and cooled. The sludge caused by the sludge may cause the temperature in the tank to become uneven, reducing thermal efficiency, or the steam may directly heat the sludge contained during digestion, causing the death of microorganisms due to the heat. There are many problems in terms of efficiency.

この考案は、槽内に中吊り状に立設したドラフ
トチユーブ内に汚泥投入管、蒸気吹込管及び撹拌
ガス吹込管を挿入開口させることにより、汚泥を
その投入時において加温すると共にこれを消化中
の汚泥中に撹拌混入させて、前述した問題を解決
し、熱効率、混合撹拌効率が良く、消化能力の高
い消化槽を提供することを目的とするものであ
る。
This idea heats the sludge when it is introduced and digests it by inserting and opening a sludge inlet pipe, a steam blowing pipe, and a stirring gas blowing pipe into a draft tube suspended in the tank. The purpose of this invention is to solve the above-mentioned problems by stirring and mixing it into the sludge inside, and to provide a digestion tank with good thermal efficiency, mixing and stirring efficiency, and high digestive capacity.

以下、この考案の実施例について図面を参照し
て説明する。
Hereinafter, embodiments of this invention will be described with reference to the drawings.

図において、1は消化槽本体で、その中央部に
は大径のドラフトチユーブ2がステー3により支
持され中吊り状に立設されている。ドラフトチユ
ーブ2内の上部中央には本体1の天井部1aを貫
通して汚泥投入管4が挿入開口4aされ、その開
口部4aには下方に向けて投入管4より若干大径
の案内管4bが設けられている。汚泥投入管4内
にはその管壁の一部を貫通して加温用の蒸気吹込
管5が挿入され、その下端はドラフトチユーブ2
の下部中央に開口5aされている。また、前記汚
泥投入管4の外側、即ち案内管4bとドラフトチ
ユーブ2との間隙6内には、その円周方向に所要
の間隔をおいて複数の撹拌用のガス送入管7,7
が槽本体の天井部1aを貫通して挿入され、その
下端のガス吐出部7aがドラフトチユーブ2の上
下の中間部に位置するように設けられている。
In the figure, reference numeral 1 denotes a digester main body, and a large-diameter draft tube 2 is supported by a stay 3 and erected in the center of the main body. A sludge input pipe 4 is inserted into the opening 4a in the upper center of the draft tube 2 through the ceiling 1a of the main body 1, and a guide pipe 4b having a slightly larger diameter than the input pipe 4 is inserted downward into the opening 4a. is provided. A steam blowing pipe 5 for heating is inserted into the sludge input pipe 4 through a part of its wall, and its lower end is connected to the draft tube 2.
An opening 5a is provided at the center of the lower part of the opening 5a. Further, on the outside of the sludge input pipe 4, that is, in the gap 6 between the guide pipe 4b and the draft tube 2, a plurality of stirring gas supply pipes 7, 7 are provided at required intervals in the circumferential direction.
is inserted through the ceiling portion 1a of the tank body, and the gas discharge portion 7a at the lower end thereof is located at an intermediate portion between the upper and lower sides of the draft tube 2.

次に、以上のように構成された消化槽の作動に
ついて説明する。消化槽の正常な運転時には、撹
拌用ガスはガス送入管7から送られその吐出部か
らドラフトチユーブ2内に噴出されて上昇する。
この噴出されたガスの上昇力によつて槽内の液は
点線矢印のように循環されることになる。その
際、蒸気吹込管5から加温用蒸気が供給され、そ
の開口部5aから液中に噴出される。それによつ
てドラフトチユーブ2内を通る循環液は全体的に
加温され、ドラフトチユーブ2の上部から槽内へ
流出されることになる。一方、槽内へ新たに供給
される汚泥は、汚泥投入管4によつてドラフトチ
ユーブ2の上部内へ供給されるが、それまでの間
に蒸気吹込管4の周辺を通過するので若干予備加
温されてドラフトチユーブ2内に流入し、ドラフ
トチユーブ2の中央部を蒸気吹込管4に沿つて下
降する。その際、蒸気によつて加温された循環流
との接触により或は蒸気により、直接或は間接に
温められ、やがてドラフトチユーブ2内の循環上
昇流に混入してその上部から槽内へ流出されるの
である。
Next, the operation of the digestion tank configured as above will be explained. During normal operation of the digester, stirring gas is sent from the gas feed pipe 7 and is ejected from its discharge portion into the draft tube 2 and rises.
Due to the upward force of this ejected gas, the liquid in the tank is circulated as shown by the dotted arrow. At this time, heating steam is supplied from the steam blowing pipe 5 and is ejected into the liquid from the opening 5a. As a result, the circulating fluid passing through the draft tube 2 is heated as a whole and flows out from the upper part of the draft tube 2 into the tank. On the other hand, sludge newly supplied into the tank is supplied into the upper part of the draft tube 2 through the sludge input pipe 4, but since it passes around the steam blowing pipe 4 in the meantime, it undergoes some preliminary processing. The heated steam flows into the draft tube 2 and descends through the center of the draft tube 2 along the steam blowing pipe 4. At that time, it is heated directly or indirectly by contact with the circulating flow heated by the steam, and eventually mixes with the circulating upward flow in the draft tube 2 and flows out from the upper part into the tank. It will be done.

以上説明したように、この考案は、槽内に中吊
り状に立設したドラフトチユーブ内において、そ
の中央下部に蒸気吹込管を挿入開口させると共
に、その上部には汚泥投入管を開口させ、該汚泥
投入管とドラフトチユーブとの間には撹拌用ガス
送入管の吐出部を設け、撹拌と加温と汚泥の供給
とを、かなり限定された広さのドラフトチユーブ
内において同時的に行なうようにしたので、槽内
に供給される汚泥は、その初めにおいて加温され
るために熱効率がよく、しかも槽内温度の均一化
が図れると共に、供給汚泥と槽内循環汚泥との混
合撹拌効率も向上される。また、蒸気によつて消
化中に含まれる汚泥を直接加温することが少ない
ため、微生物が熱により死滅する割合が減少する
等、全体として消化効率を大巾に向上させること
ができるという効果が得られる。
As explained above, this device has a draft tube suspended in the tank, a steam blowing pipe is inserted and opened at the lower center of the draft tube, and a sludge input pipe is opened at the upper part of the draft tube. A discharge part of the stirring gas supply pipe is installed between the sludge input pipe and the draft tube, so that stirring, heating, and sludge supply can be performed simultaneously within the fairly limited draft tube. As a result, the sludge supplied into the tank is heated at the beginning, so it has good thermal efficiency, and the temperature inside the tank can be made uniform, and the mixing and agitation efficiency of the supplied sludge and the circulating sludge inside the tank can be improved. Improved. In addition, since the steam does not directly heat the sludge contained during digestion, the rate at which microorganisms die due to heat is reduced, and overall digestion efficiency can be greatly improved. can get.

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

図面はこの考案の一実施例の要部を示す縦断面
図である。 1……消化槽本体、2……ドラフトチユーブ、
4……汚泥投入管、5……蒸気吹込管、7……撹
拌用ガス吹込管。
The drawing is a longitudinal cross-sectional view showing a main part of an embodiment of this invention. 1...Digestion tank body, 2...Draft tube,
4... Sludge input pipe, 5... Steam blowing pipe, 7... Stirring gas blowing pipe.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 槽内に中吊り状に立設したドラフトチユーブ内
において、その中央下部に蒸気吹込管を挿入開口
させると共に、その上部には、前記蒸気吹込管を
囲んで設けた汚泥投入管を開口させ、該汚泥投入
管とドラフトチユーブとの間には撹拌用ガス送入
管の吐出部を設けたことを特徴とする、消化槽。
In a draft tube suspended in the tank, a steam blowing pipe is inserted and opened at the lower center of the draft tube, and a sludge input pipe surrounding the steam blowing pipe is opened at the upper part of the draft tube. A digestion tank characterized in that a discharge part of a stirring gas supply pipe is provided between a sludge input pipe and a draft tube.
JP1981142696U 1981-09-28 1981-09-28 Digestion tank Granted JPS5848400U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1981142696U JPS5848400U (en) 1981-09-28 1981-09-28 Digestion tank

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1981142696U JPS5848400U (en) 1981-09-28 1981-09-28 Digestion tank

Publications (2)

Publication Number Publication Date
JPS5848400U JPS5848400U (en) 1983-04-01
JPS62800Y2 true JPS62800Y2 (en) 1987-01-09

Family

ID=29935714

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1981142696U Granted JPS5848400U (en) 1981-09-28 1981-09-28 Digestion tank

Country Status (1)

Country Link
JP (1) JPS5848400U (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2994441B1 (en) * 2012-08-13 2017-02-10 Michel Bonhomme MAINLY ANAEROBIC, CONTINUOUS, MULTI-PHASE, POLYSUBTRAT, FERMENTATION PROCESS AND PLANT IN THICK MATERIAL
JP6204764B2 (en) * 2013-09-06 2017-09-27 水ing株式会社 Methane fermentation treatment equipment

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5617501Y2 (en) * 1972-05-08 1981-04-23
JPS4911429U (en) * 1972-05-08 1974-01-31

Also Published As

Publication number Publication date
JPS5848400U (en) 1983-04-01

Similar Documents

Publication Publication Date Title
US4790289A (en) Sediment agitating apparatus for water heater
US4753220A (en) Direct contact water heater
JPS62800Y2 (en)
US4416254A (en) Flue structure for domestic heating equipment
CN106732290A (en) A kind of reactor of continuous production nitromethane
US4126420A (en) Hydrolysis column for an ammonium diuranate conversion line processing system
US4803957A (en) Gas/liquid heat exchanger
CN205807394U (en) There is the CFBC equipment of Even air distribution device
CN214863398U (en) Material melting configuration system for preventing hot gas backflow
CN111023812B (en) A feeding system for a waste can and waste aluminum foil briquetting furnace
CN207362234U (en) Enzymatic vessel
CN209917896U (en) Reation kettle is used in water treatment agent production
CN223826806U (en) A waste heat recovery device for recycled lead smelting flue gas
EP0029041B1 (en) A universal furnace
CN206996549U (en) A kind of bitumen blowing reactor
CN113145021A (en) Material melting configuration system for preventing hot gas backflow
TW202604647A (en) High-temperature atomization hydrolysis system with pressure relief device
CN216282038U (en) Energy-concerving and environment-protective nature biomass boiler
JPH1036862A (en) Coarse gas cooler
CN217844858U (en) A temperature-controllable bathing water supply system for coal mines
CN213159450U (en) Beasts and birds traditional chinese veterinary medicine extract concentrator
CN213120063U (en) Homogenizing equipment with bidirectional circulating wind direction
CN222469027U (en) A catalytic hydrogenation device
JPS635836Y2 (en)
CN104561543B (en) Axial flow biological oxidation reactor with bundling pipes