JPH04169819A - Bubble tube type apparatus for detecting liquid level - Google Patents

Bubble tube type apparatus for detecting liquid level

Info

Publication number
JPH04169819A
JPH04169819A JP29783290A JP29783290A JPH04169819A JP H04169819 A JPH04169819 A JP H04169819A JP 29783290 A JP29783290 A JP 29783290A JP 29783290 A JP29783290 A JP 29783290A JP H04169819 A JPH04169819 A JP H04169819A
Authority
JP
Japan
Prior art keywords
gas
bubble tube
liquid level
tank
digestion
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
Application number
JP29783290A
Other languages
Japanese (ja)
Inventor
Hisayuki Kako
久幸 加来
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.)
Yaskawa Electric Corp
Original Assignee
Yaskawa Electric Corp
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 Yaskawa Electric Corp filed Critical Yaskawa Electric Corp
Priority to JP29783290A priority Critical patent/JPH04169819A/en
Publication of JPH04169819A publication Critical patent/JPH04169819A/en
Pending legal-status Critical Current

Links

Landscapes

  • Measurement Of Levels Of Liquids Or Fluent Solid Materials (AREA)

Abstract

PURPOSE:To attain prevention of crevice corrosion of a stainless steel member, and others, by a method wherein a rare gas such as nitrogen or argon which is inactive for a digestive process and does not contain oxygen except as an impurity is employed as a gas to be used for purge inside a bubble tube. CONSTITUTION:A gas of 50% N2 - 50% Ar stored 3 as a gas for purge is supplied to a constant flow rate controller 7 through a filter 4, a pressure reducing unit 5 and a pressure gage 6. While the flow rate thereof is monitored by a flowmeter 8, the gas is sent to a bubble tube 2 at a prescribed flow rate by a gas-sending pipe 9 and released as bubbles into a digestion tank 1 from the fore end of the tube. Since the gas for purge sent into the bubble tube 2 does not contain oxygen except as an impurity, it does not cause corrosion of a member formed of stainless steel in the tank 1, either form an oxygen concentration cell between the lower part of a sticking substance and the outside even when a floating matter due to sewage treatment sticks on the stainless steel member, thus enabling prevention of crevice corrosion. Since a rare gas such as nitrogen, He, Ne, Ar, etc. produces no effect on a digestive process, besides, the conditions of the sewage treatment can be maintained.

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は下水処理において有機物の分解を目的として行
われる微生物による嫌気性消化のための消化タンク内の
液位を検出する気泡管式液位検出装置に関する。
Detailed Description of the Invention [Industrial Application Field] The present invention is a bubble tube type liquid level detection system for detecting the liquid level in a digestion tank for anaerobic digestion using microorganisms for the purpose of decomposing organic matter in sewage treatment. This invention relates to a detection device.

[従来の技術] 従来、密閉されたタンク内の液位を検出する場合に気泡
管式液位検出装置が用いられているが、この液位検出装
置は、たとえば第5図に示すように、タンク1内に気泡
管2を挿入し、フィルター4を通した空気を、減圧器5
および圧力計6を介して定流量調節器7で流量を一定に
保持させて送気管9で気泡管2に送り、気泡管先端から
液中に気泡として放出させ、そのときの管内の背圧で液
位を検出すようにしている。8は流量計、10は止め弁
である。すなわち、このときの管内の背圧Pは P=H+Pa (H・タンク内の液位に相当する空気の静圧)(Pa:
気泡管先端における空気の静圧)であり、Paが流速に
比例するので、空気の流量を一定に保持させることによ
り、絞り弁11を介して圧力変換器12から液位信号1
3を得ることができる。
[Prior Art] Conventionally, a bubble tube type liquid level detection device has been used to detect the liquid level in a sealed tank. A bubble tube 2 is inserted into the tank 1, and the air that has passed through the filter 4 is transferred to a pressure reducer 5.
Then, the flow rate is kept constant with a constant flow regulator 7 via a pressure gauge 6, and the air is sent to the bubble tube 2 through the air supply tube 9, and is released as bubbles into the liquid from the tip of the bubble tube, and the back pressure inside the tube at that time It is designed to detect the liquid level. 8 is a flow meter, and 10 is a stop valve. That is, the back pressure P inside the pipe at this time is P=H+Pa (H・Static pressure of air corresponding to the liquid level in the tank) (Pa:
The static pressure of the air at the tip of the bubble tube) and Pa is proportional to the flow velocity.
You can get 3.

また、特開昭59−83017号公報にも従来の例とし
て同様のものが示されており、この公報には放射性廃液
を扱う液体貯槽の液位検出装置として、パージ用の気体
が外部に放出されないようにしたもので、タンク内のパ
ージ用気体を吸引するためのポンプをそなえ、このポン
プの下流側Iこ流量調節器を設けて流量を制御し、パー
ジ管を介してタンク内に気体を戻すようにしたものが提
案されている。
A similar conventional example is also disclosed in Japanese Patent Application Laid-Open No. 59-83017, which describes a liquid level detection device for a liquid storage tank that handles radioactive waste liquid, in which purge gas is released to the outside. It is equipped with a pump to suck the purge gas in the tank, and a flow rate regulator is provided downstream of this pump to control the flow rate, and the gas is sucked into the tank through the purge pipe. A proposal has been made to bring it back.

このような気泡管式の液位検出装置では、一般に腐食防
止のため、気泡管をオーステナイトステンレス鋼で構成
している。
In such a vial type liquid level detection device, the vial is generally made of austenitic stainless steel to prevent corrosion.

下水処理における嫌気性汚泥消化タンクは、嫌気性条件
下で微生物の作用を利用するため、タンク内の消化ガス
の成分は、通常メタン60〜65%、二酸化炭素33〜
35%、水素0〜2%、硫化水素001〜0.02%、
窒素0〜3%と言われており、消化タンク内の処理液の
PHは7.2〜7.4程度の中性に維持されているが、
消化ガスに腐食性の硫化水素(H2S)  が存在する
ので、一般のものと同様に、気泡管や温度計用保護管、
撹拌用インペラ、加熱用蒸気吹込管など消化タンク内の
部材には、5US304や5US316などのオーステ
ナイト系ステンレス鋼が用いられている。
Anaerobic sludge digestion tanks used in sewage treatment utilize the action of microorganisms under anaerobic conditions, so the components of the digestion gas in the tank are usually 60-65% methane and 33-33% carbon dioxide.
35%, hydrogen 0-2%, hydrogen sulfide 001-0.02%,
It is said that the nitrogen content is 0-3%, and the pH of the processing solution in the digestion tank is maintained at a neutral level of about 7.2-7.4.
Since corrosive hydrogen sulfide (H2S) is present in the digestion gas, please use bubble tubes, thermometer protection tubes,
Austenitic stainless steels such as 5US304 and 5US316 are used for parts inside the digestion tank, such as the stirring impeller and the heating steam blowing pipe.

E発明が解決しようとする課題] ステンレス鋼の耐食性は、表面の不働態皮膜によって維
持されており、酸素が十分に存在する条件や、酸素が全
(存在しない環境で接触している液が中性であれば腐食
を生じ難いが、下水処理における消化タンク内の処理液
には浮遊物が多く含まれており、この浮遊物が液面に近
いステンレス部材の表面に付着しやすく、このような状
態で気泡管から空気を放出すると、付着物の下部と外部
との間に酸素濃淡電池が形成され、付着物の下部に激し
い隙間腐食を生じ、この腐食速度が早いため短期間で気
泡管に貫通孔が形成され、この孔から空気が抜けて液位
の検出値に誤差を生じる欠点がある5、 また、液位検出のために気泡管に空気を吹き込むと、嫌
気性の条件に維持されている消化タンク内の汚泥処理条
件の平衡がくずれて、有機物の分解が安定に行われなく
なる問題がある。
[Problems to be solved by the invention] The corrosion resistance of stainless steel is maintained by a passive film on the surface, and the corrosion resistance of stainless steel is maintained under conditions where there is sufficient oxygen or when the liquid in contact with it is in an environment where there is no oxygen. However, in sewage treatment, the treated liquid in the digestion tank contains many suspended solids, and these suspended solids tend to adhere to the surface of stainless steel parts near the liquid surface. If air is released from the vial under such conditions, an oxygen concentration cell will be formed between the bottom of the deposit and the outside, causing severe crevice corrosion at the bottom of the deposit, and as this corrosion rate is fast, the vial will be damaged in a short period of time. The disadvantage is that a through hole is formed, and air escapes through this hole, causing an error in the detected value of the liquid level5.Also, when air is blown into the bubble tube to detect the liquid level, anaerobic conditions are maintained. There is a problem that the equilibrium of the sludge treatment conditions in the digestion tank is disrupted, and the decomposition of organic matter becomes unstable.

本発明は、このような下水処理における特殊事情にかん
がみ、消化タンク内のステンレス部材に隙間腐食を生じ
ることがな(、処理条件にも影響を与えないようにした
気泡管式液位検出装置を提供することを目的とする。
In view of the special circumstances in sewage treatment, the present invention has developed a bubble tube type liquid level detection device that does not cause crevice corrosion on the stainless steel members in the digestion tank (and does not affect the treatment conditions). The purpose is to provide.

[課題を解決するための手段] このため、気泡管内のパージに用いられる気体として、
消化タンク内の消化作用に不活性で、不純物として以外
には酸素を含まない窒素およびHe、Ne、Arなどの
希ガスの少なくとも1種からなる気体を使用する。
[Means for solving the problem] For this reason, as a gas used for purging inside the bubble tube,
For the digestion action in the digestion tank, a gas is used which is inert and does not contain oxygen except as an impurity and is composed of nitrogen and at least one rare gas such as He, Ne, Ar, etc.

また、パージ用の気体として、消化タンク内の消化作用
によって生じた気体を取り出して加圧し、流量を調整し
て用いることができる。この場合、気泡管周囲の液面を
覆う仕切り室から気体を取り出すようにしたり、消化タ
ンク内の気体を脱硫装置を通すことによって腐食性ガス
を除去して取り出すようにすることが望ましい。
Further, as a purge gas, the gas generated by the digestion action in the digestion tank can be taken out and pressurized, and the flow rate can be adjusted and used. In this case, it is desirable to extract the gas from a partition that covers the liquid surface around the bubble tube, or to remove the corrosive gas by passing the gas in the digestion tank through a desulfurization device.

[作用コ したがって、気泡管に送り込まれるパージ用気体は、実
質的に酸素を含んでおらず、タンク内のステンレス鋼で
構成された部材の腐食が防止され、下水処理による浮遊
物がステンレス部材に付着しても、付着物下部と外部と
の酸素濃淡電池を形成することがなく、隙間腐食を生じ
ない。
[Effects] Therefore, the purge gas sent into the bubble tube does not substantially contain oxygen, which prevents corrosion of the stainless steel components in the tank, and prevents suspended matter from sewage treatment from forming on the stainless steel components. Even if it adheres, it does not form an oxygen concentration cell between the lower part of the deposit and the outside, and crevice corrosion does not occur.

また、窒素や前記の希ガスは、いずれも消化タンク内の
消化作用に全(影響を与えないので、消化タンク内に吹
き込まれても、汚泥処理条件を損なうことがない。
Furthermore, since neither nitrogen nor the above-mentioned rare gases have any effect on the digestion action in the digestion tank, they do not impair the sludge treatment conditions even if they are blown into the digestion tank.

なお、消化タンク内の気体を用いる場合に、脱硫装置を
介して硫化ガスを除去させ、定流量調節器や圧力変換器
などの腐食を防止する。
In addition, when using the gas in the digestion tank, sulfide gas is removed via a desulfurization device to prevent corrosion of constant flow regulators, pressure converters, etc.

[実施例] 以下、図に示す実施例について説明する。[Example] The embodiment shown in the figures will be described below.

第1図の実施例において、1は消化タンク、2は気泡管
で、パージ用気体として貯蔵タンク3に貯蔵された50
%N250%Arガスを、フィルター4、減圧器5、お
よび圧力計6を介して定流量調節器7に供給し、流量計
8で流量を監視しながら送気管9により止め弁10を介
して一定の流量で気泡管2に送り、気泡管先端からタン
ク内に気泡として放出させる。
In the embodiment shown in FIG. 1, 1 is a digestion tank, 2 is a bubble tube, and 500 ml of gas is stored in a storage tank 3 as a purge gas.
%N250%Ar gas is supplied to a constant flow regulator 7 via a filter 4, a pressure reducer 5, and a pressure gauge 6, and the flow rate is monitored by a flow meter 8 while being controlled at a constant rate by an air supply pipe 9 via a stop valve 10. It is sent to the bubble tube 2 at a flow rate of , and released as bubbles into the tank from the tip of the bubble tube.

この時の気泡管の背圧を、絞り弁11を通して圧力変換
器12で測定し、液位信号13に変換する。検出後の圧
力変換器内のガスは弁14で大気中に放出される。なお
、2]、はタンク内の汚泥、22は気泡管を囲む防波管
、23は撹拌インペラ、24は撹拌モータ、25は加熱
用蒸気吹込管、26は温度計で、防波管その他の部材は
すべてステンレス鋼SUS 3 Q 4で構成されてい
る。
The back pressure in the bubble tube at this time is measured by a pressure transducer 12 through a throttle valve 11 and converted into a liquid level signal 13. The gas in the pressure transducer after detection is released into the atmosphere by the valve 14. In addition, 2] is the sludge in the tank, 22 is the breakwater tube surrounding the bubble tube, 23 is the stirring impeller, 24 is the stirring motor, 25 is the heating steam blowing pipe, 26 is the thermometer, and the breakwater tube and other All members are made of stainless steel SUS3Q4.

このように構成された本実施例の検出装置を用いて1年
間の操業を行った結果、ステンレス部材には全く腐食が
認められず、表面の付着物は消化タンク内の浮遊物と同
じ黒色を早し、ていた。
As a result of one year of operation using the detection device of this example configured in this way, no corrosion was observed on the stainless steel components, and the deposits on the surface were black, the same color as the floating matter in the digestion tank. It was early.

これに対して、比較のため同じ構成の消化タンクでパー
ジ用気体として空気を用いたものでは、1年間の操業で
、気泡管や防波管の水面付近に浮遊物が固X付着し、こ
の部分の下部に貫通孔が発生し、液位の検出値に誤差を
生じていた。また、パージ気体に含まれている酸素によ
って硫化水素が酸化され、硫黄を生成して付着物の表面
が黄色を呈しており、嫌気性の処理条件に変化が認めら
れた。
On the other hand, for comparison, in a digestion tank with the same configuration using air as the purge gas, after one year of operation, suspended matter adhered to the water surface of the bubble tube and breakwater pipe, and this A through hole had occurred at the bottom of the part, causing an error in the detected liquid level. In addition, hydrogen sulfide was oxidized by the oxygen contained in the purge gas, producing sulfur, which turned the surface of the deposits yellow, indicating a change in the anaerobic treatment conditions.

なお、前述の実施例では、パージ気体として50%N2
−50%Ar ガスを用いているが、これに限られるも
のではなく、不純物として以外には実・質的に酸素を含
まない希ガスであればよく、He、Ne、Ar、Kr、
Xe、Rnおよび窒素の少なくとも1種からなるガスを
使用することにより同様の効果が得られる。
In addition, in the above-mentioned example, 50% N2 was used as the purge gas.
-50% Ar gas is used, but it is not limited to this, and any rare gas that does not substantially or qualitatively contain oxygen other than as an impurity may be used, such as He, Ne, Ar, Kr,
A similar effect can be obtained by using a gas consisting of at least one of Xe, Rn, and nitrogen.

第2図は別の実施例で、第1図の実施例と同じ部分に同
一の符号を付している。15はコンプレッサ、16は吸
気管、17は圧力変換器12からの戻し管である。
FIG. 2 shows another embodiment, in which the same parts as in the embodiment of FIG. 1 are given the same reference numerals. 15 is a compressor, 16 is an intake pipe, and 17 is a return pipe from the pressure converter 12.

消化タンク1内上部の消化作用によって生じたガスを吸
気管16を介して取り出し、コンプレッサ15で圧縮加
圧してフィルター4および減圧器5を通して圧力調整し
、定流量調節器7に供給する。流量計8で流量を監視し
ながら一定流量で送気管9により気泡管2に送られたガ
スは、先端からタンク内に放出される。この時の圧力変
換器12に加わるガス圧を測定し、液圧信号13に変換
する。検出後のガスは戻し管17でタンク内に戻される
Gas generated by the digestion action in the upper part of the digestion tank 1 is taken out through the intake pipe 16, compressed and pressurized by the compressor 15, pressure-regulated through the filter 4 and pressure reducer 5, and supplied to the constant flow regulator 7. The gas is sent to the bubble tube 2 through the air supply pipe 9 at a constant flow rate while monitoring the flow rate with the flow meter 8, and is discharged into the tank from the tip. The gas pressure applied to the pressure transducer 12 at this time is measured and converted into a hydraulic pressure signal 13. The gas after detection is returned into the tank through a return pipe 17.

また、第3図に示すように消化タンク内の防波管ととも
に気泡管の周囲の液面を覆ってガス採集室18を設け、
このガス採集室内で得られる消化作用による汚泥中から
の消化ガスを、吸気管16から取り出すようにすれば、
コンプレッサに送られる気体と気泡管から放出される気
体の成分が同様になり、消化タンク内の嫌気性処理条件
に与える影響がなくなる。19はガス採集室内の圧力調
整弁である。
In addition, as shown in FIG. 3, a gas collection chamber 18 is provided to cover the liquid surface around the bubble tube together with the breakwater in the digestion tank.
If the digestion gas from the sludge resulting from the digestion action obtained in the gas collection chamber is taken out from the intake pipe 16,
The composition of the gas sent to the compressor and the gas released from the bubble tube are the same, and there is no effect on the anaerobic treatment conditions in the digestion tank. 19 is a pressure regulating valve in the gas collection chamber.

第4図は、消化タンク内の消化ガスを用いる場合に、消
化ガスに含まれている腐食性硫化ガスによる装置の腐食
を防止するようにしたもので、吸気管16にNaOH溶
液を使用した脱硫装置20を設けている。したがって、
消化タンク1から取り出されて、コンプレッサ15に送
られる消化ガスに含まれている硫化水素やメルカプタン
類などの腐食性硫化ガスを捕集除去して、装置を腐食か
ら防止する。なお、脱硫装置20は消化タンク1に取り
付けるようにしてもよく、実施例に示したNaOH溶液
のものに限られるものではない。
Figure 4 shows a system that prevents corrosion of the equipment due to the corrosive sulfide gas contained in the digestion gas when using the digestion gas in the digestion tank. A device 20 is provided. therefore,
Corrosive sulfide gases such as hydrogen sulfide and mercaptans contained in the digestion gas taken out from the digestion tank 1 and sent to the compressor 15 are collected and removed to prevent the equipment from corrosion. Note that the desulfurization device 20 may be attached to the digestion tank 1, and is not limited to the one for the NaOH solution shown in the embodiment.

[発明の効果] このように本発明によれば、気泡管内のパージ用気体と
して、消化作用に対して不活性で、不純物として以外に
は酸素を含まない窒素および希ガスの少なくとも1種か
らなる気体を使用しているため、消化タンク内のステン
レス部材の局部的な腐食を確実に防止でき、長期間にわ
たって検出液位の誤差がな(、信頼性の高い気泡管式液
位針を提供できるとともに、嫌気性処理条件を変化させ
ることがなく安定した汚泥処理を行うことができる効果
が得られる。
[Effects of the Invention] As described above, according to the present invention, the purge gas in the bubble tube is made of at least one of nitrogen and rare gas, which is inert to the digestive action and does not contain oxygen except as an impurity. Since gas is used, local corrosion of the stainless steel parts in the digestion tank can be reliably prevented, and there is no error in the detected liquid level over a long period of time (and a highly reliable bubble tube type liquid level needle can be provided). At the same time, it is possible to perform stable sludge treatment without changing the anaerobic treatment conditions.

なお、パージ用気体として、消化タンク内の気体を用い
ることにより、別個にパージ用気体を準備する必要がな
く、貯蔵タンクも不要になる効果があり、また、脱硫装
置を設けて、消化タンク内の気体に含まれている腐食性
ガスを捕集させることにより、液位検出のための配管や
器具にオーステナイト系ステンレス鋼などの耐腐食性に
優れた材料を用いる必要がなく、加工が容易な銅合金な
どを用いられるとともに、液位検出回路に気体の漏れを
生じた場合にも、電気回路などを腐食させるおそれがな
い利点がある。
In addition, by using the gas in the digestion tank as the purge gas, there is no need to prepare a separate purge gas and there is no need for a storage tank. By collecting the corrosive gas contained in the gas, there is no need to use materials with excellent corrosion resistance such as austenitic stainless steel for piping and equipment for liquid level detection, and the process is easy. Copper alloy or the like is used, and there is an advantage that even if gas leaks from the liquid level detection circuit, there is no risk of corrosion of the electric circuit or the like.

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

第1図は本発明の実施例を示す構成図、第2図は他の実
施例を示す構成図、第3図は第2図を改良した実施例の
一部断面図、第4図は別の実施例を示す構成図、第5図
は従来の例を示す構成図である。 1は消化タンク、2は気泡管、3は貯蔵タンク、4はフ
ィルター、5は減圧器、6は圧力計、7は定流量調節器
、8は流量計、12は圧力変換器、13は液位信号、1
8はガス採集室、20は脱硫装置、21は汚泥、22は
防波管、23は撹拌インペラ、24は撹拌モータ、25
は加熱用蒸気吹込管、26は温度計である。 特許出願人 株式会社 安用電機製作所乙    1 第3 図 とυ 第4 図
Fig. 1 is a block diagram showing an embodiment of the present invention, Fig. 2 is a block diagram showing another embodiment, Fig. 3 is a partial sectional view of an embodiment improved from Fig. 2, and Fig. 4 is a separate diagram. Fig. 5 is a block diagram showing a conventional example. 1 is a digestion tank, 2 is a bubble tube, 3 is a storage tank, 4 is a filter, 5 is a pressure reducer, 6 is a pressure gauge, 7 is a constant flow regulator, 8 is a flow meter, 12 is a pressure transducer, 13 is a liquid position signal, 1
8 is a gas collection chamber, 20 is a desulfurization device, 21 is sludge, 22 is a breakwater pipe, 23 is a stirring impeller, 24 is a stirring motor, 25
2 is a heating steam blowing pipe, and 26 is a thermometer. Patent applicant Yasuyo Electric Manufacturing Co., Ltd. 1 Figure 3 and υ Figure 4

Claims (1)

【特許請求の範囲】 1 微生物の嫌気性消化によって汚泥の処理を行う下水
処理用密閉消化タンクに設けた気泡管に、一定流量の気
体を送って、気泡管の先端から気泡として放出させ、管
内の背圧を測定してタンク内の液位を検出する気泡管式
液位検出装置において、気泡管に送るパージ用気体とし
て、消化作用に対して不活性で、不純物として以外には
酸素を含まない窒素および希ガスの少なくとも1種から
なる気体を使用することを特徴とする気泡管式液位検出
装置。 2 微生物の嫌気性消化によって汚泥の処理を行う下水
処理用密閉消化タンクに設けた気泡管に、一定流量の気
体を送って、気泡管の先端から気泡として放出させ、管
内の背圧を測定してタンク内の液位を検出する気泡管式
液位検出装置において、気泡管内のパージ用気体として
、消化作用によって生じたタンク内の気体を用いること
を特徴とする気泡管式液位検出装置。 3 前記パージ用気体が、気泡管の周囲に設けた液面を
覆う仕切り室で採集された気体である請求項2記載の気
泡管式液位検出装置。 4 前記パージ用気体が、消化タンク内の消化作用によ
って生じた気体を、脱硫装置を介して取り出すことを特
徴とする請求項2または3記載の気泡管式液位検出装置
[Scope of Claims] 1. A constant flow of gas is sent to a bubble tube installed in a sealed digestion tank for sewage treatment that processes sludge by anaerobic digestion of microorganisms, and the gas is released as bubbles from the tip of the bubble tube, and the gas inside the tube is released. In a bubble tube type liquid level detection device that detects the liquid level in a tank by measuring the back pressure of A bubble tube liquid level detection device characterized in that it uses a gas consisting of at least one of nitrogen and rare gases. 2. A constant flow of gas is sent to a bubble tube installed in a closed digestion tank for sewage treatment, where sludge is treated by anaerobic digestion of microorganisms, and the gas is released as bubbles from the tip of the bubble tube, and the back pressure inside the tube is measured. 1. A bubble tube type liquid level detection device for detecting a liquid level in a tank by using a bubble tube type liquid level detection device, characterized in that gas in the tank generated by a digestive action is used as a purge gas in the bubble tube. 3. The vial type liquid level detection device according to claim 2, wherein the purge gas is gas collected in a partition provided around the vial and covering the liquid level. 4. The bubble tube type liquid level detection device according to claim 2 or 3, wherein the purge gas is gas generated by a digestion action in a digestion tank and is extracted through a desulfurization device.
JP29783290A 1990-11-01 1990-11-01 Bubble tube type apparatus for detecting liquid level Pending JPH04169819A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP29783290A JPH04169819A (en) 1990-11-01 1990-11-01 Bubble tube type apparatus for detecting liquid level

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP29783290A JPH04169819A (en) 1990-11-01 1990-11-01 Bubble tube type apparatus for detecting liquid level

Publications (1)

Publication Number Publication Date
JPH04169819A true JPH04169819A (en) 1992-06-17

Family

ID=17851733

Family Applications (1)

Application Number Title Priority Date Filing Date
JP29783290A Pending JPH04169819A (en) 1990-11-01 1990-11-01 Bubble tube type apparatus for detecting liquid level

Country Status (1)

Country Link
JP (1) JPH04169819A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100255459B1 (en) * 1997-11-04 2000-05-01 유성용 Drain water level measuring method of a recaimed land
JP2005274147A (en) * 2004-03-22 2005-10-06 Fujitsu Ltd Liquid level detection device and medical fluid treatment device
CN102012247A (en) * 2010-10-27 2011-04-13 江苏科技大学 Blowing level meter with flow and temperature compensation functions
JP2021089183A (en) * 2019-12-03 2021-06-10 栗田工業株式会社 Measurement device and measurement method for in-tank liquid level

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100255459B1 (en) * 1997-11-04 2000-05-01 유성용 Drain water level measuring method of a recaimed land
JP2005274147A (en) * 2004-03-22 2005-10-06 Fujitsu Ltd Liquid level detection device and medical fluid treatment device
JP4571422B2 (en) * 2004-03-22 2010-10-27 富士通セミコンダクター株式会社 Liquid level detection device and chemical treatment device
CN102012247A (en) * 2010-10-27 2011-04-13 江苏科技大学 Blowing level meter with flow and temperature compensation functions
JP2021089183A (en) * 2019-12-03 2021-06-10 栗田工業株式会社 Measurement device and measurement method for in-tank liquid level

Similar Documents

Publication Publication Date Title
ATE183832T1 (en) MIXING AND MEASURING SYSTEM FOR A MULTIPHASE PROCESS
US20140262984A1 (en) Determining biofilm thickness in a membrane supported biofilm reactor
JPH04169819A (en) Bubble tube type apparatus for detecting liquid level
Stenstrom et al. Theory to practice: Oxygen transfer and the new ASCE standard
CN103952657B (en) Ferrous sulfide gas phase passivation device
CN111252943A (en) Sulfur removal skid-mounted device and method in high-sulfur-content oil field sewage combined station
EP0274246A1 (en) Measuring apparatus
JP4982106B2 (en) Water quality inspection system
CA2323920A1 (en) Methods and apparatus for monitoring water process equipment
Muraki et al. Effects of chromium content up to 5% and dissolved oxygen on CO2 corrosion
CN112682542A (en) Improved liquid level pressure tapping structure of torch water-sealed tank
JP3368868B2 (en) Conductivity meter and acid concentration continuous measurement device
JPS5850462A (en) Measurement of dissolved oxygen concentration for oxygen activated sludge method
JPH02290987A (en) Method for predicting corrosion of metal in water system
CN217384833U (en) A airtight sampling device for trimethylchlorosilane
JP2971646B2 (en) Gas analyzer
CN217484278U (en) Anti-siphon structure for outlet discharge of flow cell
CN213875099U (en) Pump suction type gas analysis and detection device
JPS6014747Y2 (en) Odor control equipment in the chemical district of a coke manufacturing plant
Bich et al. Corrosion in MDEA Gas Treating Plants: Correlation Between Laboratory Testing and Field Experience
JPH0650855A (en) Break through detecting method and device for device for eliminating harmful object in exhaust gas
JP3398507B2 (en) Auxiliary cooling system
CN117054602A (en) VOCs monitoring method
RU2173813C1 (en) Method of detection of defects in pipelines in pouring liquefied gases for prevention of spillage
JPS607786Y2 (en) Gas dissolving device that dissolves gas in liquid