JPS61257289A - Controlling method for airflow of air compressor - Google Patents

Controlling method for airflow of air compressor

Info

Publication number
JPS61257289A
JPS61257289A JP9679385A JP9679385A JPS61257289A JP S61257289 A JPS61257289 A JP S61257289A JP 9679385 A JP9679385 A JP 9679385A JP 9679385 A JP9679385 A JP 9679385A JP S61257289 A JPS61257289 A JP S61257289A
Authority
JP
Japan
Prior art keywords
air
compressor
fed
reaction
butterfly valve
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
JP9679385A
Other languages
Japanese (ja)
Inventor
Yoshihiko Morishita
森下 良彦
Yukio Sasaki
幸雄 佐々木
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.)
JFE Engineering Corp
Original Assignee
NKK Corp
Nippon Kokan 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 NKK Corp, Nippon Kokan Ltd filed Critical NKK Corp
Priority to JP9679385A priority Critical patent/JPS61257289A/en
Publication of JPS61257289A publication Critical patent/JPS61257289A/en
Pending legal-status Critical Current

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  • Treatment Of Water By Oxidation Or Reduction (AREA)

Abstract

PURPOSE:To always permit appropriate control of air flow to be fed to a wet oxidizing device by measuring continuously oxygen concn. in the exhaust air discharged after completion of the reaction and feeding back the measured results to a butterfly valve provided before a compressor for feeding air. CONSTITUTION:When desulfurizing liquid of coke oven gas, several urban waste water or industrial waste water is oxidized with air at high temp. and under high pressure in a wet oxidizing device 3, the concn. of oxygen in the exhaust gas discharged after completion of the reaction is measured continuously, and the measured results are fed back to a butterfly valve 6 provided before a compressor for feeding air to control thus the amt. of the air to be fed. Thus, the amt. of the air to be fed to the wet oxidizing device is always controlled appropriately, and the oxidation efficiency is held stably and the power of the air compressor can be saved. Accordingly, stabilization of operation is realized by this method, and an economically rational process is provided.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、;−クス炉ガスの脱硫装置から発生する廃液
や生活排水、産業廃水などを空気により高温・高圧下で
酸化させ、硫安母液として回収したシ、含有する有害物
を無害化する湿式酸化装置等における空気圧縮機の風量
制御方法に関するものである。
[Detailed Description of the Invention] [Field of Industrial Application] The present invention oxidizes waste liquid, domestic wastewater, industrial wastewater, etc. generated from a desulfurization equipment for -gas furnace gas with air at high temperature and high pressure to produce ammonium sulfate mother liquor. The present invention relates to a method for controlling the air volume of an air compressor in a wet oxidation device, etc., which detoxifies the harmful substances contained in the collected waste.

〔従来の技術〕[Conventional technology]

湿式酸化装置等における空気圧縮機の風量制御方法とし
ては、大別して連続式のものと段階的に行うものとがあ
る◎ さらに具体的には (1)  バイパス弁によ〕圧縮空気を吸気側に一部戻
す方法 (2)圧縮機駆動源の回転数を変更する方法、(3)各
段の吸気弁を開放することKよって制御する方法、 などがある。
Air volume control methods for air compressors in wet oxidation equipment, etc. can be roughly divided into continuous methods and step-by-step methods. More specifically, (1) compressed air is transferred to the intake side using a bypass valve. There are two methods: (2) a method of changing the rotation speed of the compressor drive source; (3) a method of controlling by opening the intake valves of each stage.

そして、これらの方法は、湿式酸化装置の立地操業条件
その他によ〕適宜採用されている。
These methods are adopted as appropriate depending on the location and operating conditions of the wet oxidation apparatus.

〔発明が解決しようとする問題点〕[Problem that the invention seeks to solve]

ところで、上述のような従来の形式の制御方法にはそれ
ぞれ次のようカ問題点を抱えていた。
However, each of the conventional control methods described above has the following problems.

すなわち、 (1)  バイパス弁により圧縮空気の一部または全部
を吸気側に戻す方法は、100〜0%というli囲を無
段階でしかも連続的に風量の調1節−を行うことが可能
であるが空気〜圧縮機の負荷社変らず駆動用動力の損失
が大きい。
In other words, (1) The method of returning part or all of the compressed air to the intake side using a bypass valve makes it possible to steplessly and continuously adjust the air volume within the range of 100% to 0%. However, the loss of driving power is large regardless of the load of the air compressor.

(2)圧縮機駆動源の回転数を変更する方法は、スヂー
ムおよびヂーゼル駆動用としてはあるが、電導駆動用は
装置が複雑となると共に改造費用の面かち利用しKくい
(2) A method of changing the rotational speed of the compressor drive source is available for swivel and diesel drives, but it is difficult to use for conductive drives due to the complexity of the equipment and the cost of modification.

(3)各段の吸気弁を開閉し制御する方法は、空気また
は油圧により吸気弁の全部または半分を開放するもので
あるため、その調節量は0%、50%、100%のよう
に不連続な段階的なものであシ負荷変動に対して連続的
な微調整を行うことができない。
(3) The method of opening/closing and controlling the intake valves at each stage is to open all or half of the intake valves using air or hydraulic pressure, so the amount of adjustment is variable such as 0%, 50%, and 100%. Since it is a continuous step-by-step method, it is not possible to make continuous fine adjustments to load fluctuations.

というものである。That is what it is.

そのほか空気圧縮機の出口(すなわち系内の入口側5r
:Jけられている圧力調整弁を開き、系内に装入する以
前の段階で放風して空気量を調整する方法もある。しか
し、空気圧縮機後の空気量調整であることから圧縮機k
かかる動力を減少させることができない欠点がある。
In addition, the outlet of the air compressor (i.e. the inlet side 5r of the system)
: There is also a method of opening the pressure regulating valve that is closed and blowing air before charging into the system to adjust the amount of air. However, since the air volume is adjusted after the air compressor, the compressor k
There is a drawback that such power cannot be reduced.

〔問題点を解決するための手段〕[Means for solving problems]

本発明は、上述の如き・従来法における次点を排除し、
必要な際に所望の量だけの空気を送ることの可能な方法
を確立すべく種々検討を加えた結果、反応終了後排出さ
れる排気中の酸素濃度を連続計測し、その結果を空気圧
縮機にフィードバックさせ′供給空気量を制御すること
を特徴とする空気圧縮機の風量制御方法に到達したもの
”である。
The present invention eliminates the runner-up problems in the conventional method as described above,
As a result of various studies to establish a method that can send the desired amount of air when needed, we continuously measured the oxygen concentration in the exhaust gas discharged after the reaction, and the results were sent to an air compressor. This is a method for controlling the air volume of an air compressor, which is characterized by controlling the amount of air supplied by feeding back the information.

〔作用〕[Effect]

本発明は、反応終了後排出される排気中の酸素濃度を連
続測定して湿式酸化装置等への酸素供給量の調節を空気
圧縮機の前に設けたバタフライ弁によって行うものであ
る。
In the present invention, the oxygen concentration in the exhaust gas discharged after the completion of the reaction is continuously measured, and the amount of oxygen supplied to the wet oxidizer or the like is adjusted using a butterfly valve provided in front of the air compressor.

酸化効率を判定する場合、従来反応完了後の液の性状(
例えtfscN%81 o、 )を滴定法外どの分析を
利用していたが、測定に時間を要し測定頻度が限定され
るため現時点での状況を把握することは殆ど不可能に近
い。また、供給空気量の調整ができないため、酸化効率
の悪化をまねいたシ、過剰空気供給を行う場合が多い。
When determining oxidation efficiency, conventionally the properties of the liquid after the reaction is completed (
For example, tfscN%81o, ) was analyzed using methods other than titration, but it takes time to measure and the measurement frequency is limited, making it almost impossible to grasp the current situation. Furthermore, since the amount of air supplied cannot be adjusted, excessive air supply is often required, leading to deterioration of oxidation efficiency.

本発明の風量制御方法は、吸込みストレーナと空気圧縮
機との間の管路にバタフライ弁を設けると共に、反応終
了後の排ガス中の酸素濃度を測定する酸素濃度計のプロ
ーブを排ガス洗浄塔に設けて、プローブによって検知さ
れた排気ガス中の酸素濃度のデータを演算器に入力し、
予め設定されているプログラムによって前記バタフライ
弁の開閉を自動調節して空気量を制御するものである。
In the air volume control method of the present invention, a butterfly valve is installed in the pipeline between the suction strainer and the air compressor, and an oxygen concentration meter probe is installed in the exhaust gas cleaning tower to measure the oxygen concentration in the exhaust gas after the reaction is completed. input the oxygen concentration data in the exhaust gas detected by the probe into the computer,
The amount of air is controlled by automatically adjusting the opening and closing of the butterfly valve according to a preset program.

〔実施例〕〔Example〕

以下、本発明方法を実際のコークス炉ガス脱硫液湿式酸
化装置に応用して操業した例を図面によって示し、その
構成および効果を具体的に説明する。
Hereinafter, an example in which the method of the present invention is applied to an actual coke oven gas desulfurization liquid wet oxidation apparatus will be shown with reference to the drawings, and its configuration and effects will be specifically explained.

第1図は、本発明に従って構成した湿式酸化装置周辺の
空気流路を示した概略図であシ、1は空気吸い込みスト
レーナ、2は圧縮機、6は湿式酸化装置、4はスクラバ
、5は酸素濃度計、6は調節弁(バタフライ弁)、7は
演算処理装置である。
FIG. 1 is a schematic diagram showing an air flow path around a wet oxidizer constructed according to the present invention, in which 1 is an air suction strainer, 2 is a compressor, 6 is a wet oxidizer, 4 is a scrubber, and 5 is a 6 is a control valve (butterfly valve), and 7 is an arithmetic processing unit.

図示していないが、スクラバ4の上方の気体室には排ガ
ス中酸素濃度検出用のプループが挿入されておシ、この
プローブから酸素濃度計5に情報を伝え、ここで数量化
を図ったのち、演算処理装置7Vc信号を出力するよう
罠なっている。
Although not shown, a probe for detecting the oxygen concentration in the exhaust gas is inserted into the gas chamber above the scrubber 4. Information is transmitted from this probe to the oxygen concentration meter 5, where it is quantified. , the arithmetic processing unit 7 is configured to output a Vc signal.

この演算処理装置7で入力信号を処理したのち、予め設
定されているプログラムに沿って調節弁6の開閉を命令
する信号を発して調節弁6の開閉を行わせるようKm成
している0 調節弁6の開閉駆動源は、空気圧によっても良いし油圧
方式であってもよい・ 次に、空気吸い込みストレーナ1で吸い込んだ風量t−
調節弁6で調節した際には、吐出弁の温度上昇と吸い込
み圧力の増大が当然に考えられる。
After processing the input signal in this arithmetic processing unit 7, a signal is issued to command the opening and closing of the regulating valve 6 according to a preset program, and the control valve 6 is controlled to open and close. The driving source for opening and closing the valve 6 may be pneumatic or hydraulic. Next, the air volume t- sucked in by the air suction strainer 1 is
When adjusting with the control valve 6, it is naturally thought that the temperature of the discharge valve and the suction pressure will increase.

この関係を確認するために、例えは第2図にその概略を
示したような水平対向型圧縮機を用いてその1段目の弁
における温度上昇の程度を調査したO なお第2図中、1.1・・・Vはそれぞれ1段目。
In order to confirm this relationship, we investigated the degree of temperature rise at the first stage valve using a horizontally opposed compressor as schematically shown in Figure 2. 1.1...V is the first stage.

2段目・・・5段目の圧縮機を示し、T11T!・・・
T・は吐出弁を示したものであって、この吐出弁は図示
していないが2段目以降の圧縮機にも設けられている。
2nd stage... Indicates the 5th stage compressor, T11T! ...
T. indicates a discharge valve, and although this discharge valve is not shown, it is also provided in the second and subsequent stage compressors.

表の結果から明らかなように、1段目吐出弁の温度上昇
は、6弁を測定しても高くて120℃程度であシ、実際
の操業に際しては特に高い温度には当らないものであシ
設備上問題にならないことが判った。
As is clear from the results in the table, the temperature rise of the first-stage discharge valve is only about 120°C at most when measuring six valves, which is not a particularly high temperature during actual operation. It turned out that there was no problem with the equipment.

一力、吸込圧力につhて吸込弁(バタフライ弁〕、  
 の調節を行わないもの忙比較して、行ったものは駆動
用動力の減少が大きいことが認められる。
In terms of suction pressure, suction valve (butterfly valve),
It is recognized that the reduction in driving power is greater in the case where the adjustment is made, compared to the case where the adjustment is not made.

〔発明の効果〕〔Effect of the invention〕

氷見F!Aを実施することにより、湿式酸化装置Kに供
給する空気量を常に適正に調節することが可能となシ、
酸化効率の安定維持ができると共に空気圧縮機の動力を
節約することか可能となった。
Himi F! By implementing A, it is possible to always appropriately adjust the amount of air supplied to the wet oxidizer K.
It has become possible to maintain stable oxidation efficiency and to save power for the air compressor.

従って、この方法は、操業の安定化が図れると共に経済
的にも合理的な方法であるということができる。
Therefore, this method can be said to be an economically rational method that can stabilize the operation.

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

第1図は、湿式酸化装置の周辺機器を示した概略図、第
2図は空気圧縮機の組合せを示した概略図である。 1・・・吸込みストレーナ、2・・・圧縮機、3・・・
湿式酸化装置、4・・・スクラバ、5・・・酸素濃度計
、6・・・調節弁、7・・・演算装置。
FIG. 1 is a schematic diagram showing peripheral equipment of a wet oxidation apparatus, and FIG. 2 is a schematic diagram showing a combination of air compressors. 1... Suction strainer, 2... Compressor, 3...
Wet oxidizer, 4...Scrubber, 5...Oxygen concentration meter, 6...Control valve, 7...Arithmetic device.

Claims (1)

【特許請求の範囲】[Claims] 湿式酸化装置によりコークス炉ガスの脱硫液や各種生活
排水および産業排水を高温高圧下で空気酸化させる際、
反応終了後排出される排気中の酸素濃度を連続計測し、
その結果を空気供給圧縮機前に設けたバタフライ弁にフ
ィードバックさせて供給空気量を制御することを特徴と
する空気圧縮機の風量制御方法。
When using wet oxidation equipment to air oxidize coke oven gas desulfurization liquid and various domestic and industrial wastewater under high temperature and high pressure,
After the reaction is complete, the oxygen concentration in the exhaust gas is continuously measured.
A method for controlling air volume of an air compressor, characterized in that the result is fed back to a butterfly valve provided in front of the air supply compressor to control the amount of air to be supplied.
JP9679385A 1985-05-09 1985-05-09 Controlling method for airflow of air compressor Pending JPS61257289A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP9679385A JPS61257289A (en) 1985-05-09 1985-05-09 Controlling method for airflow of air compressor

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP9679385A JPS61257289A (en) 1985-05-09 1985-05-09 Controlling method for airflow of air compressor

Publications (1)

Publication Number Publication Date
JPS61257289A true JPS61257289A (en) 1986-11-14

Family

ID=14174512

Family Applications (1)

Application Number Title Priority Date Filing Date
JP9679385A Pending JPS61257289A (en) 1985-05-09 1985-05-09 Controlling method for airflow of air compressor

Country Status (1)

Country Link
JP (1) JPS61257289A (en)

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