JPS6323797A - Methane sedimentation tank having methane bacteria immobilizing carrier take-out apparatus - Google Patents
Methane sedimentation tank having methane bacteria immobilizing carrier take-out apparatusInfo
- Publication number
- JPS6323797A JPS6323797A JP61167316A JP16731686A JPS6323797A JP S6323797 A JPS6323797 A JP S6323797A JP 61167316 A JP61167316 A JP 61167316A JP 16731686 A JP16731686 A JP 16731686A JP S6323797 A JPS6323797 A JP S6323797A
- Authority
- JP
- Japan
- Prior art keywords
- tank
- methane
- sedimentation tank
- valve
- manhole
- 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
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 title claims abstract description 26
- 238000004062 sedimentation Methods 0.000 title claims abstract description 13
- 230000003100 immobilizing effect Effects 0.000 title abstract description 3
- 241000894006 Bacteria Species 0.000 title description 4
- 238000000855 fermentation Methods 0.000 claims abstract description 12
- 230000004151 fermentation Effects 0.000 claims abstract description 12
- 239000000969 carrier Substances 0.000 claims description 3
- 230000001580 bacterial effect Effects 0.000 claims description 2
- 238000007689 inspection Methods 0.000 claims 2
- 239000007788 liquid Substances 0.000 abstract description 12
- 238000000034 method Methods 0.000 abstract description 4
- 238000005192 partition Methods 0.000 abstract 2
- 239000010802 sludge Substances 0.000 description 14
- 235000020083 shōchū Nutrition 0.000 description 4
- 239000002699 waste material Substances 0.000 description 3
- 238000007796 conventional method Methods 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 239000005416 organic matter Substances 0.000 description 2
- 239000000919 ceramic Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
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
Landscapes
- Apparatus Associated With Microorganisms And Enzymes (AREA)
- Biological Treatment Of Waste Water (AREA)
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
- Treatment Of Sludge (AREA)
Abstract
Description
【発明の詳細な説明】
(イ) 産業上の利用分野
この発明は、本格焼酎廃液メタン醗酵に於いて、醗酵槽
の次に位置する沈降槽に閏するものである。DETAILED DESCRIPTION OF THE INVENTION (a) Industrial Application Field The present invention is applied to a sedimentation tank located next to a fermentation tank in full-scale shochu waste liquid methane fermentation.
(ロ) 従来の技術
メタン醗酵槽の後にメタン沈降(3設ける目的は、rr
3泥を重力で圧密沈降させ、A送ポン1で醗酵槽に戻し
ながら次第に醗酵槽内の汚泥濃度を高くして行く事にあ
る。(b) The purpose of installing methane sedimentation (3) after the conventional technology methane fermentation tank is to
3. The sludge is consolidated and settled by gravity, and is returned to the fermentation tank by the A pump 1, gradually increasing the sludge concentration in the fermentation tank.
しかしながら、この重力沈降法では、沈降槽の汚泥濃度
は、精々2す、川10 PPM位で、これを返送して得
た醗酵槽内汚泥濃度は、15.01111 PPM位に
止まる。However, in this gravity settling method, the sludge concentration in the settling tank is at most about 2 PPM, and the sludge concentration in the fermentation tank obtained by returning the sludge is only about 15.01111 PPM.
従って、醗酵槽に於ける処理可能の有機物のfA度は、
31]、11111J P回位が限度であり、有機物
濃度が100.000 P門もある本格焼酎廃液に対し
ては、従来法では全く通用しないのが現状である。Therefore, the fA degree of organic matter that can be processed in the fermenter is:
31], 11111J The current situation is that conventional methods are completely inapplicable to genuine shochu waste liquid, which has a maximum concentration of 100,000 P and an organic matter concentration of 100,000 P.
(ハ) 発明が解決しようとする問題点。(c) Problems that the invention attempts to solve.
従来法では、汚泥a度が15.1illU PPMを越
す辺りから、沈降槽より汚泥の流口が始まり、精々21
1、問II P四位か限度となるが、これは嫌気性汚泥
菌の特長として菌体が活性汚泥菌に比べて。In the conventional method, the sludge flow starts from the sedimentation tank when the sludge a degree exceeds 15.1 illU PPM, and at most 21
1.Question II P4 is the limit, but this is a feature of anaerobic sludge bacteria compared to activated sludge bacteria.
極めて小さくて軽く、少しの動きにも影響される為であ
る。This is because it is extremely small and light, and is affected by even the slightest movement.
この様な汚泥を流口から防ぐ目的で、固定化担体でメタ
ン菌を固定化す・る事により、次第に沈降槽内の汚&濃
度分高くして、 ?1LSS ら40.υnu PP
M以上を得る事が出来、更に、この高濃度汚泥含醜酵槽
に返送する事により1本格焼酎廃液の醗酵処理を可能に
した訳である。In order to prevent such sludge from entering the flow outlet, by immobilizing methane bacteria with an immobilization carrier, the concentration of sludge in the sedimentation tank will gradually increase. 1LSS et al. 40. υnu PP
It was possible to obtain more than M, and furthermore, by returning the highly concentrated sludge to the fermentation tank, it became possible to ferment the 1st Honkaku Shochu waste liquid.
り5が、これ等の担体は、浅く広く開放型の活性汚泥沈
澱槽と対象的な2深く細く密閉型の沈降槽の下部に充填
されている為、担体表面の有孔性劣1ヒ等に依る収り替
え、取り出しての菌体検査、付着状況の観察等を行うと
しても構造上困難である。However, since these carriers are filled at the bottom of a deep, narrow, and closed type settling tank, which is in contrast to a shallow, wide open activated sludge settling tank, the porosity of the carrier surface is poor. Due to its structure, it would be difficult to replace the container, inspect the bacterial cells after removing it, and observe the state of adhesion.
ス、取り替える時は、沈降槽内の液を抜き出した?褒、
深い槽内で危険を犯して作業する以外に方法が無い状態
である。So, when replacing it, did you drain the liquid from the sedimentation tank? Reward,
There is no other option but to risk working in a deep tank.
本発明が、解決しようとする問題、へは、次の様な横道
により簡単に槽外よつ醗酵運転を中止する事なく、担体
等を取り出す事が出来る装置にある。The problem to be solved by the present invention lies in an apparatus that can easily take out carriers and the like without stopping the fermentation operation using the following side route.
(ニ)問題点と解決するための手段
この光明念、メタン沈降槽の収り出し装置として実施し
た実施例を、図面第1図にもとずいて説明する。(d) Problems and means for solving them An embodiment of this invention, which was implemented as a device for discharging methane settling tanks, will be explained based on FIG. 1 of the drawings.
第112により、沈降槽を上部J’JIと下部槽4に分
け、メタ/槽からの流入管3に接続している沈降槽の中
心を通る整流筒2は、上部槽の1ぞ閉蓋16より下がっ
てト一部槽のほぼ中央迄沖びている。According to No. 112, the settling tank is divided into an upper J'JI and a lower tank 4, and the rectifying tube 2 passing through the center of the settling tank connected to the inflow pipe 3 from the meta/tank is connected to It is lower and extends offshore almost to the center of the tank.
上部+11と下部槽4とは、仕切弁等を取り1=tける
に充5rな間隔があり、整流筒2には仕切弁7とバイパ
ス弁8が収り付けである。There is a sufficient distance between the upper part +11 and the lower tank 4, which is 1 = 5 r, including gate valves, etc., and a gate valve 7 and a bypass valve 8 are housed in the rectifying cylinder 2.
更に、上部槽と下部槽の上下槽を結ぶ配管6が整流筒2
の回りにあり、その配管の各々に仕切弁9が取り付けで
ある。Furthermore, a pipe 6 connecting the upper and lower tanks of the upper tank and the lower tank is connected to the rectifier tube 2.
A gate valve 9 is attached to each of the pipes.
(ホ) 作用
今、メタン醗酵運転中に担体5を収り出す場合、先ず、
整流筒2の仕切弁7を閉にして、バイパス弁8と關け、
更に、配管6の仕切弁9を閉にする。(E) Function When removing carrier 5 during methane fermentation operation, first,
Close the gate valve 7 of the rectifier tube 2, connect it to the bypass valve 8,
Furthermore, the gate valve 9 of the pipe 6 is closed.
そうして、マンホールIIIより槽内液がこぼれない様
に、液面計12を見ながら返送ポンプ11でメタン沈降
槽内の液な引き抜き、液位がマンホールlliよりrが
ったら開けて担体5を取り出す。Then, while watching the liquid level gauge 12, draw out the liquid in the methane sedimentation tank with the return pump 11 so that the liquid in the tank does not spill from manhole III. When the liquid level is higher than manhole lli, open the tank and remove the carrier 5. Take out.
上部槽lと下部Jf4は、7と9の仕切弁により遮断し
てあり、又、り流面2のバイパス弁8は開けであるので
、メタン醗酵の運転は、中断する事なく作業が出来る訳
である。The upper tank L and the lower Jf4 are shut off by gate valves 7 and 9, and the bypass valve 8 on the flow surface 2 is open, so the methane fermentation operation can be carried out without interruption. It is.
(へ) 発明の効果
実施例より、この方法によると本格焼酎葵溜IJE m
f) ’%合合力汚泥濃度、MLSS 311.lI
l+J 〜35.1jllll PPMとなり、高負荷
運転が可能となった。(f) Effects of the invention According to the examples, according to this method, authentic shochu Aoi Tame IJE m
f) '% resultant sludge concentration, MLSS 311. lI
l+J ~35.1jlll PPM, making high load operation possible.
4、 [;lit而の簡単な説明
図は、この発明の沈降槽の実施例を示すもので、第11
2は実施例の縦断面図である。4. A simple explanatory diagram showing an embodiment of the sedimentation tank of the present invention.
2 is a longitudinal sectional view of the embodiment.
1 上部槽 2 整流筒 3 流入管 4 下部槽 5 袋詰めしたセラミック有孔担体 6 上下つなぎ配管 7 仕切弁〈バタフライ弁) 8 バイパス弁(バタフライ弁) 9 仕切弁(バタフライ弁) 10 マンホール II iA送ポンプ 12 液面計 13 上滑Z^排出管 14 バイパス管 15 越流■ノlチ 16 密閉蓋1 Upper tank 2. Rectifier tube 3 Inflow pipe 4 Lower tank 5. Bagged ceramic porous carrier 6 Top and bottom connecting piping 7 Gate valve (butterfly valve) 8 Bypass valve (butterfly valve) 9 Gate valve (butterfly valve) 10 Manhole II iA feed pump 12 Liquid level gauge 13 Upper slide Z^ discharge pipe 14 Bypass pipe 15 Overflow■ Nolchi 16 Sealing lid
Claims (1)
槽を結ぶ配管に各々仕切弁を設けて、必要時に遮断し下
部槽に充填されている固定化担体をマンホールより取り
出して、菌体検査点検等がメタン醗酵運転中に可能とし
た装置を有する沈降槽。[Scope of Claims] The sedimentation tank is divided into an upper tank and a lower tank, and a rectifying cylinder that passes through the center of the lower tank from the upper tank, and a gate valve are provided in each of the pipes connecting the upper tank and the lower tank. A sedimentation tank equipped with a device that can be shut off at times, and the immobilized carriers filled in the lower tank can be taken out from a manhole to perform bacterial cell inspection and other inspections during methane fermentation operation.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP61167316A JPS6323797A (en) | 1986-07-16 | 1986-07-16 | Methane sedimentation tank having methane bacteria immobilizing carrier take-out apparatus |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP61167316A JPS6323797A (en) | 1986-07-16 | 1986-07-16 | Methane sedimentation tank having methane bacteria immobilizing carrier take-out apparatus |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS6323797A true JPS6323797A (en) | 1988-02-01 |
Family
ID=15847488
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP61167316A Pending JPS6323797A (en) | 1986-07-16 | 1986-07-16 | Methane sedimentation tank having methane bacteria immobilizing carrier take-out apparatus |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6323797A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5122455A (en) * | 1989-03-03 | 1992-06-16 | International Reagents Corporation | Got isozyme assay |
JP2014237104A (en) * | 2013-06-10 | 2014-12-18 | 中国電力株式会社 | Water purifier |
KR20160131105A (en) | 2014-05-08 | 2016-11-15 | 미쯔비시 레이온 가부시끼가이샤 | Wadding |
-
1986
- 1986-07-16 JP JP61167316A patent/JPS6323797A/en active Pending
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5122455A (en) * | 1989-03-03 | 1992-06-16 | International Reagents Corporation | Got isozyme assay |
JP2014237104A (en) * | 2013-06-10 | 2014-12-18 | 中国電力株式会社 | Water purifier |
KR20160131105A (en) | 2014-05-08 | 2016-11-15 | 미쯔비시 레이온 가부시끼가이샤 | Wadding |
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