JPH01194923A - Method for controlling pretreatment equipment for air separator - Google Patents
Method for controlling pretreatment equipment for air separatorInfo
- Publication number
- JPH01194923A JPH01194923A JP63017081A JP1708188A JPH01194923A JP H01194923 A JPH01194923 A JP H01194923A JP 63017081 A JP63017081 A JP 63017081A JP 1708188 A JP1708188 A JP 1708188A JP H01194923 A JPH01194923 A JP H01194923A
- Authority
- JP
- Japan
- Prior art keywords
- valve
- air separation
- adsorption tower
- separation device
- regeneration gas
- 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
Landscapes
- Separation Of Gases By Adsorption (AREA)
- Separation By Low-Temperature Treatments (AREA)
Abstract
(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は空気分離装置の前処理装置暑こ係り、特に2埼
切替式のPSA式吸e塔設備に好適な空気分離装置用地
処理装置の制御方法に関するものである。[Detailed Description of the Invention] [Industrial Application Field] The present invention relates to a pre-treatment device heat exchanger for an air separation device, and in particular, to a land treatment device for an air separation device suitable for a two-span switching type PSA type absorption tower facility. This relates to a control method.
一般に空気分離装置の前処理装置として使用されている
吸着塔設備は、その再生用のガスを空気分離装置から供
給される廃ガスによってまかなわれている。このため、
空気分離装置の起動時には再生ガスが吸着塔設備へは供
給されないため、吸着塔の精製空気出口配管より分岐さ
れたバイパス配管およびバイパス弁により蹟製空気の一
部を再生ガス用として吸着塔設備に供給している。この
バイパス弁は手動又は、溌ガスの主管圧力調節ににより
行われていた。Adsorption tower equipment, which is generally used as a pretreatment device for air separation equipment, is supplied with gas for regeneration by waste gas supplied from the air separation equipment. For this reason,
Since regeneration gas is not supplied to the adsorption tower equipment when the air separation equipment is started up, a portion of the recycled air is supplied to the adsorption tower equipment as regeneration gas using a bypass pipe and a bypass valve branched from the purified air outlet piping of the adsorption tower. supplying. This bypass valve was operated manually or by adjusting the main pipe pressure of fresh gas.
なお、この種の装置として関連するものには例えば特開
昭55−95079号が挙げられる。Note that related devices of this type include, for example, Japanese Patent Application Laid-open No. 55-95079.
上記従来技術は、空気分離装置から供給される舛
再生ガスの急激な流i1変化に婢なう圧力変動について
配置はがされておらず、吸着塔再生工程完了時に再生ガ
スが流れなくなるため急速に圧力が上昇し、また、再生
工程開始時に再生ガスが流れはじめると、急速に圧力が
降下する現象が生じ、圧力変動が制御系の外乱となると
いう課題があった。The above-mentioned conventional technology does not take into account pressure fluctuations that occur due to sudden changes in the flow rate of the regenerating gas supplied from the air separation device, and the regenerating gas stops flowing at the completion of the adsorption tower regeneration process, resulting in rapid When the pressure increases and the regeneration gas begins to flow at the start of the regeneration process, a phenomenon occurs in which the pressure rapidly decreases, causing a problem in that the pressure fluctuations cause a disturbance in the control system.
本発明の目的は、上記吸着塔の再生ガスの供給を安定さ
せると共に、精製空気のバイパス流量を最少とする空気
分離装置用前処理装置の制御方法を提供することにある
。An object of the present invention is to provide a method for controlling a pretreatment device for an air separation device, which stabilizes the supply of regeneration gas to the adsorption tower and minimizes the bypass flow rate of purified air.
上記目的は、吸着塔の切換を行う、切換制御装置から、
吸S塔のh主工程のタイミングを信号として取出し、再
生ガス圧力調節弁の出力信号の安定した時点での出力d
の大小をあらかじめ設定された値と比較し、この比較結
果をバイパス回路の弁開度設定器の出力信号に加減算す
ることにより、達成される。The above purpose is to switch the adsorption tower from the switching control device.
The timing of the h main process of the S absorption tower is taken out as a signal, and the output d is obtained when the output signal of the regeneration gas pressure control valve becomes stable.
This is achieved by comparing the magnitude of the value with a preset value and adding or subtracting the comparison result to the output signal of the valve opening setting device of the bypass circuit.
吸着塔の再生工程の開始時、完了時に生じる圧力変動を
、吸着塔切替制御装置からのタイミング信号により制御
量(再生ガス圧力調節弁の弁開反証)の不感期間を作る
ことで、吸着塔の再生ガス流坦を安定させた状態で精製
空気のバイパス流量を最少とすることができる。The pressure fluctuations that occur at the start and completion of the regeneration process of the adsorption tower can be reduced by creating a dead period for the control amount (valve opening of the regeneration gas pressure control valve) using a timing signal from the adsorption tower switching control device. The bypass flow rate of purified air can be minimized while the regeneration gas flow rate is stabilized.
以下、本発明の一実施例を第1図により説明する。 An embodiment of the present invention will be described below with reference to FIG.
図において、吸入フィルタlを通過し圧ma2で約51
ζpf/cdに圧縮された原料空気は、吸着塔3、(3
’)へ送られ、ここで後流の空気分離装置内で固化する
水分およびOO2を吸着除去し、精製空気として空気分
離装置へ送られる。一方再生ガスは公党分離装置から、
吸着塔3.(3’)へ供給され。In the figure, it passes through the suction filter l and the pressure ma2 is about 51
The raw air compressed to ζpf/cd is transferred to adsorption towers 3, (3
'), where moisture and OO2 that solidify in the downstream air separation device are adsorbed and removed, and the purified air is sent to the air separation device. On the other hand, the regeneration gas comes from the public party separation equipment.
Adsorption tower 3. (3').
該供給された再生ガスにより吸着塔3. (3’)を再
生し、再生後のガスが大気へ諺出される。吸着塔3、(
3’)の吸着工程と再生工程の切替は切替制御装置9か
らの信号により、切替弁4A、5A、4B、58.6を
開閉して行われる。二の切替運転の制御要領を9A2図
に示す。The supplied regeneration gas causes the adsorption tower 3. (3') is regenerated, and the regenerated gas is discharged to the atmosphere. Adsorption tower 3, (
The switching between the adsorption process and the regeneration process in step 3' is performed by opening and closing the switching valves 4A, 5A, 4B, and 58.6 in response to a signal from the switching control device 9. The control procedure for the second switching operation is shown in Figure 9A2.
本実施例において、空気分離装置dの起動前の状態では
、空気分離装置から再生ガスは供給されないため、バイ
パス弁8を開き、再往ガスの量を精製空気により確保し
ている。また、空気分離装置が稼動し再生ガス九が増加
した場合は、再生ガス人口配管10から吸着塔3.(3
’)を経由し大気へ放出されるので、大気までの圧力損
失が大きくなるため、p4生ガス入ロ圧力11が上昇し
、再生ガス圧力調節弁7が開放され、大気へ放出される
。このため、再生ガスの総量が再生ガス必要墓な満足し
ている場合、再生ガス圧力調節弁7が開いていることに
なる。しかし、第2図に示す如く、本再生ガス圧力調節
弁7は吸着塔3(3’)の切替工程毎に大きく開度が変
化されるため、吸S塔の切替制御装置9より1判定に適
した工程のタイミング信号を出力させる。この信号を受
けとった時間のみバイパス回路の弁の開度信号の増減を
行なうことにより、弁開度の制御を行なっている。In this embodiment, before the air separation device d is started, no regeneration gas is supplied from the air separation device, so the bypass valve 8 is opened and the amount of recirculation gas is secured by purified air. In addition, when the air separation device is in operation and the regeneration gas 9 increases, the regeneration gas artificial pipe 10 is connected to the adsorption tower 3. (3
'), the pressure loss to the atmosphere increases, so the p4 raw gas input pressure 11 increases, the regeneration gas pressure control valve 7 is opened, and the gas is discharged to the atmosphere. Therefore, when the total amount of regeneration gas satisfies the regeneration gas requirement, the regeneration gas pressure control valve 7 is open. However, as shown in FIG. 2, the opening degree of the regenerating gas pressure regulating valve 7 is greatly changed every time the adsorption tower 3 (3') is switched. Output a timing signal for an appropriate process. The valve opening degree is controlled by increasing or decreasing the opening degree signal of the valve in the bypass circuit only during the time when this signal is received.
以上の操作を行うことにより、空気分離装置の起動によ
り、徐々に再生ガス供給量が増加する毎に精製空気のバ
イパス流量を徐々に減少することができる。By performing the above operation, the bypass flow rate of purified air can be gradually reduced each time the regeneration gas supply amount gradually increases by starting the air separation device.
本実施例によれば、空気分離装置の起動時において、切
替で使用される吸着塔の再生ガスを、吸着塔の切替によ
る圧力変動等に影響されることなく、安定して供給する
ことができ、また、精製空気のバイパスrlLflを最
少にすることができる。According to this embodiment, when the air separation device is started up, the regeneration gas of the adsorption tower used for switching can be stably supplied without being affected by pressure fluctuations caused by switching the adsorption tower. , and the purified air bypass rlLfl can be minimized.
本発明によれば、精製空気を再生ガス用として利用する
場合に、再生工程開始時、または再生工程完了時の再生
ガスの供給を安定させると共に精製空気のバイパス流量
を鮫少とする効果がある。According to the present invention, when purified air is used for regeneration gas, it is possible to stabilize the supply of regeneration gas at the start of the regeneration process or at the completion of the regeneration process, and to reduce the bypass flow rate of purified air. .
第1図は本発明の一実施例の空気分離装置用前処理装置
の系統図、第2図は吸着塔の制御要領を示すタイムチャ
ート図である。
■・・・・・・吸入フィルタ、2・・・・・・圧縮&、
3.3’・・・吸着塔、4A、4B・・・・・・切
替弁(空気用)、5A。
5B・・・・・・切替弁(再生ガス用)、6・・・・・
・切替弁(加圧用)、7・・・・・・再生ガス圧力調節
弁、8・・・・・・バイパス弁、9・・・・・・切替制
御装置代理人 弁理士 小 川 勝 男・′)(j
M/図FIG. 1 is a system diagram of a pretreatment device for an air separation device according to an embodiment of the present invention, and FIG. 2 is a time chart showing a control procedure for an adsorption tower. ■・・・Suction filter, 2・・・Compression &,
3.3'...Adsorption tower, 4A, 4B...Switching valve (for air), 5A. 5B...Switching valve (for regeneration gas), 6...
・Switching valve (for pressurization), 7... Regeneration gas pressure control valve, 8... Bypass valve, 9... Switching control device representative Patent attorney Katsuo Ogawa. ′) (j M/Fig.
Claims (1)
から供給される再生ガスにより、前記吸着塔の再生を行
う空気分離装置用前処理装置の制御方法において、 空気分離装置から供給される再生ガスの圧力により大気
へ放出する弁の開度を調整し、かつ、前記弁の開度の出
力信号により、精製ガスを再生用として利用するバイパ
ス回路の弁の開度を調整し、吸着塔の再生ガスの供給を
安定させると共に精製空気のバイパス流量を最小とする
ように制御したことを特徴とする空気分離装置用前処理
装置の制御方法。 2、特許請求の範囲第1項において、制御は、吸着塔の
切替毎に大気へ放出する弁開度の出力信号が設定値より
大きい場合には前記バイパス回路の弁が閉となるよう制
御し、逆に弁開度の出力信号が設定値より小さい場合に
は前記バイパス回路の弁が開となるように制御したこと
を特徴とする空気分離装置用前処理装置の制御方法。[Scope of Claims] A method for controlling a pretreatment device for an air separation device, which uses a PSA adsorption tower with one and two towers switching type, and regenerates the adsorption tower with regeneration gas supplied from the air separation device, The opening degree of the valve that discharges to the atmosphere is adjusted by the pressure of the regeneration gas supplied from the air separation device, and the output signal of the opening degree of the valve is used to open the valve of the bypass circuit that uses the purified gas for regeneration. 1. A method for controlling a pretreatment device for an air separation device, the method comprising: controlling the flow rate of a pretreatment device for an air separation device to stabilize the supply of regeneration gas to an adsorption tower and minimize the bypass flow rate of purified air. 2. In claim 1, the control is such that the valve of the bypass circuit is closed when the output signal of the valve opening degree released to the atmosphere is larger than a set value every time the adsorption tower is switched. A method for controlling a pretreatment device for an air separation device, characterized in that, on the contrary, when the output signal of the valve opening degree is smaller than a set value, the valve of the bypass circuit is controlled to be opened.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP63017081A JPH01194923A (en) | 1988-01-29 | 1988-01-29 | Method for controlling pretreatment equipment for air separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP63017081A JPH01194923A (en) | 1988-01-29 | 1988-01-29 | Method for controlling pretreatment equipment for air separator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH01194923A true JPH01194923A (en) | 1989-08-04 |
Family
ID=11934025
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP63017081A Pending JPH01194923A (en) | 1988-01-29 | 1988-01-29 | Method for controlling pretreatment equipment for air separator |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH01194923A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2008246403A (en) * | 2007-03-30 | 2008-10-16 | Osaka Gas Co Ltd | Gas production apparatus |
-
1988
- 1988-01-29 JP JP63017081A patent/JPH01194923A/en active Pending
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2008246403A (en) * | 2007-03-30 | 2008-10-16 | Osaka Gas Co Ltd | Gas production apparatus |
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