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JPS5946680B2 - Water catcher for methane fermentation system - Google Patents
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JPS5946680B2 - Water catcher for methane fermentation system - Google Patents

Water catcher for methane fermentation system

Info

Publication number
JPS5946680B2
JPS5946680B2 JP57015120A JP1512082A JPS5946680B2 JP S5946680 B2 JPS5946680 B2 JP S5946680B2 JP 57015120 A JP57015120 A JP 57015120A JP 1512082 A JP1512082 A JP 1512082A JP S5946680 B2 JPS5946680 B2 JP S5946680B2
Authority
JP
Japan
Prior art keywords
water
gas
catcher
pipe
pressure
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
JP57015120A
Other languages
Japanese (ja)
Other versions
JPS58133892A (en
Inventor
敏一 冨岡
俊次 並河
康之 貫名
重昭 沼田
光康 小川
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Panasonic Holdings Corp
Original Assignee
Matsushita Electric Industrial Co Ltd
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 by Matsushita Electric Industrial Co Ltd filed Critical Matsushita Electric Industrial Co Ltd
Priority to JP57015120A priority Critical patent/JPS5946680B2/en
Publication of JPS58133892A publication Critical patent/JPS58133892A/en
Publication of JPS5946680B2 publication Critical patent/JPS5946680B2/en
Expired 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

【発明の詳細な説明】 本発明はメタン発酵システムにおけるガス配管中の露結
水の捕水器に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a water collector for condensation water in gas piping in a methane fermentation system.

メタン発酵システムは、メタン発酵槽、ガスタンクとガ
ス消費機器等の組み合せより成るが、それらを連結する
ガス配管が、通常都市ガス配管と大きく異る点は、発酵
ガスの方が水分含有量が多く配管中に露結水がたまりや
すいという点である。
A methane fermentation system consists of a combination of a methane fermentation tank, a gas tank, and gas consumption equipment, etc., but the gas piping that connects them is significantly different from normal city gas piping, as fermented gas has a higher water content. The problem is that condensation water tends to accumulate in the pipes.

即ち、メタン発酵槽は、メタン菌の種類にもよるが通常
30〜40℃、50〜60℃等外気より高い温度で制御
運転されている。
That is, the methane fermentation tank is normally controlled and operated at a temperature higher than the outside air, such as 30 to 40°C or 50 to 60°C, depending on the type of methane bacteria.

このためメタン発酵槽より出る発酵ガス中には、上記制
御温度のほぼ飽和水蒸気圧の水分を含んでいる。
Therefore, the fermentation gas discharged from the methane fermentation tank contains water at approximately the saturated water vapor pressure at the above-mentioned control temperature.

これが、ガスタンク、あるいはガス消費機器に至る配管
中で、外気温度に冷却され露結し、露結水は配管中に流
れ最も低い部分にたまり、配管を閉塞する。
This condensation water is cooled to outside temperature and condenses in the gas tank or in the piping leading to the gas consumption equipment, and the dew water flows into the piping and accumulates at the lowest point, blocking the piping.

上記結果により、メタン発酵槽内のガス圧が異常に上昇
したり、ガス消費機器内でガス圧に脈動を生じさせ、例
えばバーナーの炎の変動を生じさせる可能性がある等の
欠点があった。
As a result of the above results, there were drawbacks such as an abnormal increase in the gas pressure in the methane fermentation tank, or pulsations in the gas pressure in the gas consumption equipment, which could cause, for example, fluctuations in the flame of the burner. .

この欠点を補うため、乾燥剤を配管中に設け、水分除去
の方策もあるが、メタン発酵槽が実用規模のものでは、
多量の乾燥剤が必要であり、その取替えの手間も大きい
等の点から、あ寥り適当ではない。
To compensate for this drawback, there is a method to remove water by installing a desiccant in the piping, but if the methane fermentation tank is of a practical scale,
Since a large amount of desiccant is required and it takes a lot of effort to replace it, it is not suitable.

そこで、露結水を自動的かつ連続的に排除する捕水器が
用いられる場合がある。
Therefore, a water catcher that automatically and continuously removes dew condensation water is sometimes used.

第1図により上記捕水器の構造を説明すると、1はメタ
ン発酵槽、2はガスタンク、3はメタン発酵槽1かもガ
スタンク2に至る発酵ガス配管中のたわみ最下部に設け
た捕水器の水取入れ口、4は捕水器の水取入れ口3より
垂直に接続された水封管で、捕水器の水取入れ口3、水
封管4はいずれもその管内は、メタン発酵槽1内と連結
された発酵ガスで満たされている。
To explain the structure of the above water catcher with reference to Fig. 1, 1 is a methane fermentation tank, 2 is a gas tank, and 3 is a water catcher installed at the bottom of the flexure in the fermentation gas piping leading to the methane fermentation tank 1 or gas tank 2. The water intake port 4 is a water seal pipe that is vertically connected to the water intake port 3 of the water catcher, and the inside of both the water intake port 3 and the water seal pipe 4 of the water catcher is inside the methane fermentation tank 1. It is filled with fermentation gas connected to

5は捕水器本体で、その断面積は上記水封管4の断面積
よりはるかに太き(設計されている。
5 is a water catcher main body, and its cross-sectional area is much larger than the cross-sectional area of the water sealing tube 4 (as designed).

6は水封用水で、溢水ロアまで満たされ又ある。6 is water for water sealing, and is filled up to the overflowing lower part.

上記捕水器において、水封管4中の水面は、ガスタンク
20機能により加圧された発酵ガスの圧力で押し下げら
れており、捕水器本体5中の水封用水6の水面との差は
、上記発酵ガス圧の水圧換算分となる。
In the above water catcher, the water level in the water seal tube 4 is pushed down by the pressure of the fermentation gas pressurized by the gas tank 20 function, and the difference between the water level and the water level of the water seal water 6 in the water catcher main body 5 is , is the water pressure equivalent of the above fermentation gas pressure.

この事から、捕水器の水取入れ口3の高さは、発酵ガス
圧により決定される。
From this, the height of the water intake port 3 of the water catcher is determined by the fermentation gas pressure.

一方、水取入れ口3は、メタン発酵槽1、ガスタンク2
間の配管中量下部に設ける必要性から、各装置のガス管
引出し位置は上記水取入れ口3の高さに制約を受ける。
On the other hand, the water intake port 3 is connected to the methane fermentation tank 1 and the gas tank 2.
Due to the need to provide the pipes at the lower part of the pipes between the pipes, the position where the gas pipes of each device are drawn out is limited by the height of the water intake port 3.

各装置のガス管引出し位置について、さらに説明を加え
ると、ガスタンク2におい又は、水封式の場合、装置最
下部からガス管を引き出す構造上の理由により、低位置
の方が有利とされ℃いる。
To further explain the position of the gas pipe for each device, in the case of a gas tank 2 or a water seal type, a lower position is considered to be more advantageous due to structural reasons for pulling out the gas pipe from the bottom of the device. .

以上の理由により、水取入れ口の高さの低い捕水器が望
まれていた。
For the above reasons, a water catcher with a low height water intake has been desired.

本発明は、かかる要望を満足させ、かつ、配管中の露結
水の排除、異常ガス圧発生時におけるガス放出という捕
水器の目的を満たす低取入れ口捕水器を提供するもので
ある。
The present invention satisfies these needs and provides a low intake water catcher that satisfies the purpose of the water catcher: eliminating dew condensation in piping and releasing gas when abnormal gas pressure occurs.

以下、本発明の一実施例を第2図と共に説明する。An embodiment of the present invention will be described below with reference to FIG.

第2図の11は、メタン発酵槽12とガスタンク13間
の配管のたわみ最下部から分岐継手により接続された捕
水器の水取入れ口、14は上記水取入れ口より垂直に接
続された水封管で、その断面積は捕水器本体Aを構成す
る第1捕水室16の断面積よりはるかに小さく設計され
℃いる。
11 in FIG. 2 is a water intake port of a water catcher connected by a branch joint from the lowest part of the pipe between the methane fermentation tank 12 and the gas tank 13, and 14 is a water seal connected vertically from the water intake port. It is a pipe, and its cross-sectional area is designed to be much smaller than the cross-sectional area of the first water-catching chamber 16 constituting the water-catching main body A.

15は第1捕水室16内に満たされた水封用水、11は
前記水封用水15を一定水位に保つ溢水口である。
Reference numeral 15 designates water sealing water filled in the first water collection chamber 16, and reference numeral 11 designates an overflow port for keeping the water sealing water 15 at a constant water level.

18は第2捕水室1゛9内に垂直に接続された水封管で
、一端は上記捕水室19内の水封用水20中に開口し他
端は前記第1捕水室16の溢水口11に接続されている
Reference numeral 18 denotes a water sealing pipe vertically connected to the second water capturing chamber 19, one end of which opens into the water sealing water 20 within the water capturing chamber 19, and the other end of which opens into the water sealing water 20 of the first water capturing chamber 16. It is connected to the overflow port 11.

21は第2捕水室1.9中の水封用水20の水位を一定
に保つ溢水口である。
Reference numeral 21 denotes a water overflow port for keeping the water level of the water sealing water 20 in the second water collection chamber 1.9 constant.

22は前記水封管18と同様、溢水口21と第3捕水室
23中の水封用水24中に一端を開口し、他端を前記溢
水口21に接続されている。
Similar to the water seal pipe 18, the water seal pipe 22 has one end opened into the water seal water 24 in the water overflow port 21 and the third water collection chamber 23, and the other end is connected to the water overflow port 21.

25は大気圧中に開放された前記水制用水24の溢水口
である。
25 is an overflow port of the water control water 24 which is opened to atmospheric pressure.

26は一端を第1捕水室16の水封用水15中に開口し
、他端を大気中に開放した透明管より成るガス圧表示兼
補給水用管、21は上記カス圧表示兼給水用管26の埃
除は兼管中の水蒸発防止用の覆蓋で、蓋中央に小孔27
′を設けた構造である。
26 is a gas pressure display/replenishment water pipe consisting of a transparent tube with one end opened into the water sealing water 15 of the first water collection chamber 16 and the other end open to the atmosphere; 21 is a gas pressure display/supply water pipe; Dust removal from the pipe 26 is also a cover to prevent water evaporation inside the pipe, with a small hole 27 in the center of the cover.
′ is provided.

なお、上記それぞれの水封管14.18.22の水封用
水15,20,24の水面下の長さは、水取入れ口11
にかかる使用最大圧力の水圧換算分の偽より若干長く設
計されている。
In addition, the length below the water surface of the water sealing water 15, 20, 24 of each of the water sealing pipes 14, 18, and 22 is the same as that of the water intake port 11.
It is designed to be slightly longer than the water pressure equivalent of the maximum pressure used.

またガス圧表示兼補給水用管26は一端を前記水封管1
4と同じ水深で開口し、管全長は上記使用最大圧力の水
圧換算長より若干長く設計されている。
Further, the gas pressure display/replenishment water pipe 26 has one end connected to the water seal pipe 1.
It opens at the same water depth as 4, and the total length of the pipe is designed to be slightly longer than the water pressure equivalent length of the maximum pressure used above.

次に上記した捕水器の動作原理を説明する。Next, the principle of operation of the water catcher described above will be explained.

メタン発酵槽12で発生した発酵ガスは、ガスタンク内
で圧力が付加され、捕水器の水取入れ口11ではゲージ
圧P。
The fermentation gas generated in the methane fermentation tank 12 is pressurized in the gas tank, and the gauge pressure is P at the water intake port 11 of the water catcher.

mA(1あるとする。この場合、各水封管内の水面位置
は、水封用水の水面下すべてP。
mA (assuming that there is 1. In this case, the water surface position in each water seal tube is all P below the water surface of the water seal water.

/3闘に押し下げられている。従つ又第1捕水室16水
面上空隙の圧力はP。
/ It has been pushed down to 3 fights. Accordingly, the pressure in the space above the water surface of the first water capture chamber 16 is P.

−Po/3、即ち2Po/3となり、第2捕水室19水
面上空隙の圧力は2Po/3−Po/3、即ちP。
-Po/3, that is, 2Po/3, and the pressure in the space above the water surface of the second water capture chamber 19 is 2Po/3-Po/3, that is, P.

/3となる。/3.

第3捕水室23水面上空隙の圧力はPo/3−Po/3
即ち外気と等圧となる。
The pressure in the space above the water surface of the third water capture chamber 23 is Po/3-Po/3
In other words, the pressure is equal to the outside air.

上記動作により、捕水器の水取入れ口11に通常動作ガ
ス圧をかげた場合、水封管内の水面がそれぞれ一定位置
まで下った状態で静止安定して使用できる。
By the above-mentioned operation, when normal operating gas pressure is applied to the water intake port 11 of the water catcher, the water seal tube can be stably used in a state where the water level in the water seal tube is lowered to a certain position.

次に、上記発酵ガス配管中で露結した水は、配管たわみ
最下部の捕水器の水取入れ口11に集まる。
Next, the water condensed in the fermentation gas piping collects at the water intake port 11 of the water catcher at the lowest part of the pipe flexure.

上記露結水は水封管14を伝わり落ち、水封用水15中
に混合する。
The dew water flows down through the water seal pipe 14 and mixes into the water seal water 15.

混合した露結水の分だけ溢水口17より溢れ、水封管1
8を伝わり落ち、水封用水20中に混合する。
The amount of mixed dew water overflows from the overflow port 17, and the water seal pipe 1
8 and mixed into the water sealing water 20.

前記同様、混合した分だけ溢水口21より、順次溢れる
Similarly to the above, the mixed amount sequentially overflows from the overflow port 21.

この事より、水取入れ口11に集まった露神水は、溢杢
口25より溢れるという結果となる。
From this, the result is that the dew water collected at the water intake port 11 overflows from the overflow port 25.

水取入れ口11に使用最大圧力を越える異常圧がかかっ
た場合、水封管14の水面を押し下げ、発酵ガスは水封
管14の下方開口端より気泡となつ℃水封用水15中を
浮上し、第1捕水室16上部空隙に入る。
When an abnormal pressure exceeding the maximum operating pressure is applied to the water intake port 11, the water surface of the water seal tube 14 is pushed down, and the fermentation gas becomes bubbles from the lower open end of the water seal tube 14 and floats up in the temperature water seal water 15. , enters the upper space of the first water capture chamber 16.

空隙に入った発酵ガスの分だけ洗室の水封管18の水面
を押し下げ、前記同様、発酵ガスは水封管18の下方開
口端より気泡となつ℃水封用水20中を浮上し、第2捕
水室1.9、上部空隙に入る。
The water surface of the water seal tube 18 in the washing room is pushed down by the amount of fermentation gas that has entered the gap, and as described above, the fermentation gas becomes bubbles from the lower open end of the water seal tube 18 and floats up in the water seal water 20. 2 Water capture chamber 1.9 enters the upper cavity.

さらに同様にして、第3捕水室23空隙へ送られた発酵
ガスは、溢水口25より大気中へと放出される。
Furthermore, in the same manner, the fermentation gas sent to the third water capture chamber 23 gap is released into the atmosphere from the water overflow port 25.

この事から、水取入れ口11に異常圧がかかった場合、
発酵ガスは水封管14より各室を経て溢水口25より大
気中へ放出され、発酵ガスを放出する事により最大使用
圧力にまで低下する迄この放出が続けられる。
From this, if abnormal pressure is applied to the water intake port 11,
The fermentation gas is released from the water seal pipe 14 through each chamber into the atmosphere from the overflow port 25, and this release is continued until the pressure is reduced to the maximum working pressure by releasing the fermentation gas.

一方、一端を第1捕水室16内で水封管14と同じ水深
で開口し、他端を大気中に開口し、かつ第1捕水室16
上部壁を気密住良(貫通した透明管を設けた場合、水封
管14内の水面と、上記透明管中の水面との距離が、発
酵ガス圧の水圧換算分となる事を利用し透明管に目盛を
刻印し、ガス圧表示器とした。
On the other hand, one end is opened in the first water capture chamber 16 at the same water depth as the water seal tube 14, and the other end is opened to the atmosphere, and the first water capture chamber 16
The upper wall is airtight (if a transparent tube is installed, the distance between the water surface in the water seal tube 14 and the water surface in the transparent tube is equivalent to the water pressure equivalent of the fermentation gas pressure). A scale was engraved on the tube and used as a gas pressure indicator.

さらに、各捕水室内の水封用水の蒸発、逸散による減少
を補給するため、′上記透明管の大気開放端を補給水注
入口とし、前記透明管をガス圧表示兼給水管26とした
Furthermore, in order to replenish water sealing water that is reduced due to evaporation and dissipation in each water capture chamber, the open end of the transparent tube to the atmosphere was used as a replenishment water inlet, and the transparent tube was used as a gas pressure display and water supply pipe 26. .

上記のように本発明の捕水器は、施工する発酵ガス配管
が非常に低い地上高の位置であつ℃も、配管中の露結水
を連続的に、かつ自動的に排除できるという特長を有す
る。
As mentioned above, the water catcher of the present invention has the feature that dew condensation water in the piping can be continuously and automatically removed even when the fermentation gas piping to be constructed is located at a very low ground clearance and even when the piping is installed at a very low ground height. have

即ち従来の捕水器を用いる場合、特に地下構造を設けな
い限り発酵ガス圧の水圧換算分以上の地上高で配管しな
ければならないという欠点を有したのに較べ、それ以下
の高さでの配管に於い又も、従来捕水器と同様の機能が
発揮できるという特長を有する。
In other words, when using a conventional water catcher, the piping must be installed at a height above the ground equivalent to the water pressure equivalent of the fermentation gas pressure, unless an underground structure is provided. It also has the advantage that it can perform the same function as a conventional water catcher in piping.

さらに、前記第1捕水室に透明管を設ければ、発酵ガス
圧表示ができるという特長を有し他に高価な微圧計な設
置する必要がない点から、配管部材費等の節約が図れる
Furthermore, if a transparent tube is provided in the first water collection chamber, the fermentation gas pressure can be displayed, and there is no need to install an expensive micropressure gauge, which saves on piping material costs. .

なお、本発明の実施例に於いては捕水器内部を3室によ
り構成したが、室数は2以上の整数であれば理論上制限
はない。
In the embodiment of the present invention, the interior of the water catcher is configured with three chambers, but the number of chambers is theoretically not limited as long as it is an integer of two or more.

この場合、室数がふえる捏水取入れ口の高さが低(設計
できる事はいうまでもない。
In this case, it goes without saying that the height of the water inlet, which increases the number of chambers, can be designed to be low.

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

第1図は従来例の捕水器の断面図、第2図は本発明の一
実施例を示す捕水器の断面図である。 11・・・・・・水取入れ口、14・・・・・・水封管
、16・・・・・・第1捕水室、19・・・・・・第2
捕水室、23・・・・・・第3捕水室、25・・・・・
・溢水口、26・・・・・・ガス圧表示兼補給水用管、
A・・・・・・捕水器本体。
FIG. 1 is a cross-sectional view of a conventional water catcher, and FIG. 2 is a cross-sectional view of a water catcher showing an embodiment of the present invention. 11...Water intake, 14...Water seal pipe, 16...First water collection chamber, 19...Second
Water capture room, 23...Third water capture room, 25...
・Overflow port, 26...Gas pressure display and makeup water pipe,
A... Water catcher body.

Claims (1)

【特許請求の範囲】 1 メタン発酵槽、ガスタンク、発酵ガス消費機器等よ
りメタン発酵システムを構成し、前記メタン発酵槽とガ
スタンクの配管の途中に連絡した捕水器本体は、複数の
捕水室を有し、各室の溢水口を、次室の水封管と連結作
動させ、その水封管にかかる圧を室数だけ均分減圧させ
たメタン発酵システム用捕水器。 2 捕水器本体は、一端を大気中に開口し、他端を第1
の捕水室の水封用水中に水封管と同じ長さ水没させ発酵
ガス使用最高ガス圧の水圧換算長より若干長いガス圧表
示兼補給水用管を具備した特許請求の範囲第1項記載の
メタン発酵システム用捕水器。
[Scope of Claims] 1. A methane fermentation system is constituted by a methane fermentation tank, a gas tank, fermentation gas consumption equipment, etc., and a water catcher body connected in the middle of piping between the methane fermenter and the gas tank has a plurality of water catching chambers. A water catcher for a methane fermentation system, in which the overflow port of each chamber is operated in connection with the water seal pipe of the next chamber, and the pressure applied to the water seal pipe is equally reduced by the number of chambers. 2 The water catcher body has one end open to the atmosphere and the other end opened to the first
Claim 1: A gas pressure display/replenishment water pipe is submerged in the water sealing water of the water capture chamber for the same length as the water sealing pipe, and is slightly longer than the water pressure equivalent length of the maximum gas pressure used for the fermentation gas. A water catcher for the methane fermentation system described above.
JP57015120A 1982-02-01 1982-02-01 Water catcher for methane fermentation system Expired JPS5946680B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57015120A JPS5946680B2 (en) 1982-02-01 1982-02-01 Water catcher for methane fermentation system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57015120A JPS5946680B2 (en) 1982-02-01 1982-02-01 Water catcher for methane fermentation system

Publications (2)

Publication Number Publication Date
JPS58133892A JPS58133892A (en) 1983-08-09
JPS5946680B2 true JPS5946680B2 (en) 1984-11-14

Family

ID=11879958

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57015120A Expired JPS5946680B2 (en) 1982-02-01 1982-02-01 Water catcher for methane fermentation system

Country Status (1)

Country Link
JP (1) JPS5946680B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS58205568A (en) * 1982-05-24 1983-11-30 Nippon Steel Corp Painting of metallic structure excellent in shock resistance

Also Published As

Publication number Publication date
JPS58133892A (en) 1983-08-09

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