JPS625007B2 - - Google Patents

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Publication number
JPS625007B2
JPS625007B2 JP57061061A JP6106182A JPS625007B2 JP S625007 B2 JPS625007 B2 JP S625007B2 JP 57061061 A JP57061061 A JP 57061061A JP 6106182 A JP6106182 A JP 6106182A JP S625007 B2 JPS625007 B2 JP S625007B2
Authority
JP
Japan
Prior art keywords
valve
gas
regeneration gas
adsorption tower
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
JP57061061A
Other languages
Japanese (ja)
Other versions
JPS58178181A (en
Inventor
Tadashi Satono
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.)
Hitachi Ltd
Original Assignee
Hitachi 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 Hitachi Ltd filed Critical Hitachi Ltd
Priority to JP57061061A priority Critical patent/JPS58178181A/en
Publication of JPS58178181A publication Critical patent/JPS58178181A/en
Publication of JPS625007B2 publication Critical patent/JPS625007B2/ja
Granted legal-status Critical Current

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  • Separation Of Gases By Adsorption (AREA)
  • Separation By Low-Temperature Treatments (AREA)

Description

【発明の詳細な説明】 本発明は、吸着装置に係り、特に空気分離装
置、ガス分離装置等に適用するのに好適な吸着装
置に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an adsorption device, and particularly to an adsorption device suitable for application to an air separation device, a gas separation device, etc.

従来の吸着装置を第1図に示した空気分離装置
に慣用されている吸着装置により説明する。
A conventional adsorption device will be explained using an adsorption device commonly used in an air separation device shown in FIG.

第1図で、吸着塔10a,10bは、2基並列
に設置され切替え使用される。吸着塔10a,1
0bの頂部には、導管11a,11bが、底部に
は、導管12a,12bがそれぞれ連結されてい
る。導管11a,11bには、逆止弁13a,1
3bが配設された導管14と、逆止弁13c,1
3dが配設された導管15とが連結されている。
導管12a,12bには、切替弁16a,16b
が配設された導管17と、切替弁16c,16d
が配設された導管18とが連結されている。導管
14の逆止弁13a,13b間には、気体で開閉
操作される複動シリンダ駆動型の弁19aと再生
ガスを加熱する加熱器20とが設けられた再生ガ
ス供給用の導管21aが連結されている。弁19
aの前流側で導管21aから分岐し加熱器20の
後流側で導管21aに連結された再生ガス供給用
の導管21bには、気体で開閉操作される複動シ
リンダ駆動型の弁19bが設けられている。弁1
9a,19bには、気体供給用の導管22a,2
2bが連結され電気信号で開閉する電磁弁23
a,23bに連結された気体供給用の導管22c
〜22fが連結されている。再生ガス圧力調節装
置は、圧力調節計24と、再生ガス放出用の導管
25と、導管25に設けられ圧力調節計24と接
続された圧力調節弁26とで構成され、導管21
aには、圧力調節計24が設けられると共に、導
管25が連結されている。導管15の逆止弁13
c,13d間には、精製空気送出用の導管27
が、導管17の切替弁16a,16b間には、原
料空気供給用の導管28が、また、導管18の切
替弁16c,16d間には、再生ガス排出用の導
管29がそれぞれ連結されている。
In FIG. 1, two adsorption towers 10a and 10b are installed in parallel and used selectively. Adsorption tower 10a, 1
Conduits 11a and 11b are connected to the top of 0b, and conduits 12a and 12b are connected to the bottom of 0b, respectively. Check valves 13a, 1 are provided in the conduits 11a, 11b.
3b, and the check valve 13c, 1
3d is connected to the conduit 15.
Switching valves 16a, 16b are provided in the conduits 12a, 12b.
The conduit 17 in which the switching valves 16c and 16d are arranged
A conduit 18 is connected to the conduit 18. Between the check valves 13a and 13b of the conduit 14, a conduit 21a for supplying regeneration gas is connected, which is provided with a double-acting cylinder-driven valve 19a that is opened and closed by gas and a heater 20 that heats the regeneration gas. has been done. Valve 19
A regeneration gas supply conduit 21b that branches from the conduit 21a on the upstream side of the heater 20 and is connected to the conduit 21a on the downstream side of the heater 20 has a double-acting cylinder-driven valve 19b that is opened and closed by gas. It is provided. Valve 1
9a, 19b have gas supply conduits 22a, 2.
2b is connected to a solenoid valve 23 that opens and closes with an electric signal.
A gas supply conduit 22c connected to a and 23b
~22f are connected. The regeneration gas pressure regulating device is composed of a pressure regulator 24, a regeneration gas discharge conduit 25, and a pressure control valve 26 provided in the conduit 25 and connected to the pressure regulator 24.
A is provided with a pressure regulator 24 and is connected to a conduit 25. Check valve 13 for conduit 15
Between c and 13d, there is a conduit 27 for delivering purified air.
However, a conduit 28 for supplying raw air is connected between the switching valves 16a and 16b of the conduit 17, and a conduit 29 for exhausting regeneration gas is connected between the switching valves 16c and 16d of the conduit 18. .

いま、吸着塔10aが吸着工程、吸着塔10b
が再生工程にあるとすれば、切替弁16a,16
dが開放、切替弁16b,16cが閉止され、吸
着塔10aには、導管28,17,12aを経て
原料空気が供給される。吸着塔10aでは、供給
された原料空気中の水分、炭酸ガス等の不純物
(以下、不純物と略)が吸着除去される。不純物
が除去された精製空気は、吸着塔10aより逆止
弁13cを介し導管11a,15,27を経て別
途使用先へ送出される。一方、開放している電磁
弁23aを介し導管22a,22dを経て気体が
供給されることで開放される弁19aを介し導管
21aを経て加熱器20に供給され、ここで加熱
された再生ガスが逆止弁13bを介し導管21
a,14,11bを経て吸着塔10bに供給され
る。吸着塔10bは、この再生ガスで加熱再生さ
れ、再生に使用された再生ガスは、切替弁16d
を介し導管12b,18,29を経て排出され
る。吸着塔10bの加熱再生完了後、弁19a
は、電磁弁23aを介し導管22a,22cを経
て気体が供給されて閉止され、また弁19bは、
開放している電磁弁23bを介し導管22b,2
2fを経て気体が供給されて開放される。このよ
うに弁19aが閉止、弁19bが開放されると吸
着塔10bには、弁19bを介し導管21a,2
1b,21a,14を経、更に、逆止弁13bを
介し導管14,11bを経て再生ガスが供給され
る。吸着塔10bは、この再生ガスで冷却され、
冷却に使用された再生ガスは、切替弁16dを介
し導管12b,18,29を経て排出される。吸
着塔10bが所定温度まで冷却されると、弁19
bは、電磁弁23bを介し導管22b,22eを
経て気体が供給されて閉止され、これにより、吸
着塔10bへの再生ガスの供給が停止されて吸着
塔10bの再生が終了する。吸着塔10bの再生
が終了した時点で、切替弁16b,16cが開
放、16a,16dが閉止され、吸着塔10bで
は原料空気中の不純物が吸着除去され、一方、吸
着塔10aは、上記のような操作により再生され
る。なお、この場合、弁19bが閉止状態で弁1
9aが閉止されるか、逆に、弁19aが閉止状態
で弁19bが閉止されると導管21aを流通する
再生ガスの圧力が上昇するため、この圧力上昇を
圧力調節計24で検出し圧力調節計24で圧力調
節弁26が開放方向に操作されて導管25より再
生ガスが放出される。また、弁19bが閉止状態
で弁19aが開放されるが、逆に、弁19aが閉
止状態で弁19bが開放されると導管21aを流
通する再生ガスの圧力が低下するため、この圧力
低下を圧力調節計24で検出し圧力調節計24で
圧力調節弁26が閉止方向に操作されて導管25
より放出される再生ガスの量が減量されるか、又
は、放出が停止される。
Now, the adsorption tower 10a is in the adsorption process, and the adsorption tower 10b is in the adsorption process.
is in the regeneration process, the switching valves 16a, 16
d is opened, the switching valves 16b and 16c are closed, and raw air is supplied to the adsorption tower 10a through the conduits 28, 17, and 12a. In the adsorption tower 10a, impurities such as moisture and carbon dioxide gas (hereinafter abbreviated as impurities) in the supplied raw material air are adsorbed and removed. The purified air from which impurities have been removed is sent out from the adsorption tower 10a via a check valve 13c and through conduits 11a, 15, and 27 to a separate destination. On the other hand, gas is supplied via the conduits 22a and 22d through the open solenoid valve 23a, and the regeneration gas is supplied to the heater 20 via the conduit 21a through the valve 19a, which is opened, and is heated here. Conduit 21 via check valve 13b
It is supplied to the adsorption tower 10b via a, 14, and 11b. The adsorption tower 10b is heated and regenerated with this regeneration gas, and the regeneration gas used for regeneration is passed through the switching valve 16d.
via conduits 12b, 18, 29. After the heating regeneration of the adsorption tower 10b is completed, the valve 19a
is closed by supplying gas through the solenoid valve 23a and through the conduits 22a and 22c, and the valve 19b is closed.
The conduits 22b, 2 are connected via the open solenoid valve 23b.
Gas is supplied through 2f and opened. In this way, when the valve 19a is closed and the valve 19b is opened, the adsorption tower 10b is connected to the conduits 21a and 2 through the valve 19b.
Regeneration gas is supplied through conduits 14, 11b via check valve 13b. The adsorption tower 10b is cooled with this regeneration gas,
The regeneration gas used for cooling is discharged through the conduits 12b, 18, and 29 via the switching valve 16d. When the adsorption tower 10b is cooled to a predetermined temperature, the valve 19
b is closed after gas is supplied through the electromagnetic valve 23b and through the conduits 22b and 22e, thereby stopping the supply of regeneration gas to the adsorption tower 10b and completing the regeneration of the adsorption tower 10b. When the regeneration of the adsorption tower 10b is completed, the switching valves 16b and 16c are opened and the switching valves 16a and 16d are closed, and the impurities in the feed air are adsorbed and removed in the adsorption tower 10b, while the adsorption tower 10a is operated as described above. It is played back by certain operations. In this case, valve 19b is closed and valve 1 is closed.
9a is closed, or conversely, when valve 19a is closed and valve 19b is closed, the pressure of the regeneration gas flowing through conduit 21a increases. This pressure increase is detected by pressure regulator 24 and the pressure is adjusted. At step 24, the pressure regulating valve 26 is operated in the opening direction, and the regeneration gas is released from the conduit 25. Further, the valve 19a is opened while the valve 19b is closed, but conversely, when the valve 19b is opened while the valve 19a is closed, the pressure of the regeneration gas flowing through the conduit 21a decreases. The pressure regulator 24 detects the pressure, and the pressure regulator 24 operates the pressure regulating valve 26 in the closing direction, thereby opening the conduit 25.
The amount of regeneration gas released is reduced or the release is stopped.

このような吸着装置では、気体で開閉操作され
る弁の開閉速度が早く、この開閉速度に再生ガス
圧力調節装置の圧力調節速度が追従できないた
め、気体で開閉操作される弁の開閉時に再生ガス
の圧力が急激に変動し、その結果、安定して運転
ができなくなるといつた欠点があつた。
In such an adsorption device, the opening/closing speed of the valve that is operated by gas is fast, and the pressure adjustment speed of the regeneration gas pressure regulator cannot follow this opening/closing speed. The disadvantage was that the pressure of the engine fluctuated rapidly, making stable operation impossible.

なお、気体で開閉操作される弁として、この他
に単動シリンダ型の弁が用いられるる場合がある
が、この場合でも上記した欠点がある。
In addition, a single-acting cylinder type valve may be used as the valve that is opened and closed by gas, but even in this case, the above-mentioned drawbacks still exist.

本発明の目的は、上記した従来技術の欠点を解
消して、安定して運転が行える吸着装置を提供す
るものである。
An object of the present invention is to eliminate the drawbacks of the prior art described above and provide an adsorption device that can be operated stably.

本発明は、吸着装置を、再生ガスで再生される
吸着塔と、気体で開閉操作され前記吸着塔への前
記再生ガスの供給、停止を行う弁と、前記吸着塔
へ供給される前記再生ガスの圧力を検出する圧力
調節計と、該圧力調節計からの指令により前記再
生ガスで前記吸着塔への供給前に放出される再生
ガスの量を調節する圧力調節弁と、前記弁の開閉
時に前記圧力調節弁の開閉方向操作速度が追従可
能な速度に前記弁の開閉速度を調節する前記気体
の流量調節弁とを具備したものとすることで、気
体で開閉操作され吸着塔への再生ガスの供給、停
止を行う弁の開閉時に生じる再生ガスの急激な圧
力変動を抑制しようとしたものである。
The present invention provides an adsorption device including an adsorption tower that is regenerated with regeneration gas, a valve that is opened and closed by gas to supply and stop the regeneration gas to the adsorption tower, and the regeneration gas that is supplied to the adsorption tower. a pressure regulator that detects the pressure of the regenerating gas, a pressure regulating valve that adjusts the amount of regenerating gas released before the regenerating gas is supplied to the adsorption tower according to a command from the pressure regulator, and when the valve is opened and closed; The gas flow rate control valve adjusts the opening/closing speed of the valve to a speed that can be followed by the opening/closing direction operation speed of the pressure control valve, so that the regeneration gas that is opened and closed by gas is supplied to the adsorption tower. This is an attempt to suppress the rapid pressure fluctuations in the regeneration gas that occur when the valves that supply and stop the gas are opened and closed.

本発明の一実施例を第2図により説明する。な
お、第2図で、第1図と同一装置等は同一符号で
示し説明を省略する。
An embodiment of the present invention will be described with reference to FIG. Note that in FIG. 2, the same devices as in FIG.

第2図で、導管22c〜22fには、例えば、
ニードル弁等の気体の流量調節弁30a〜30d
がそれぞれ設けられている。流量調節弁30a〜
30dは、気体で開閉操作される複動シリンダ駆
動型の弁19a,19bの開閉速度を、圧力調節
計24と、導管25と、圧力調節弁26とで構成
された再生ガス圧力調節装置の圧力調節速度が追
従できる速度に調節可能である。
In FIG. 2, the conduits 22c to 22f include, for example,
Gas flow rate control valves 30a to 30d such as needle valves
are provided for each. Flow rate control valve 30a~
30d indicates the opening/closing speed of the double-acting cylinder-driven valves 19a and 19b, which are opened and closed by gas, and the pressure of the regeneration gas pressure regulating device, which is composed of a pressure regulator 24, a conduit 25, and a pressure regulating valve 26. The adjustment speed can be adjusted to a speed that can be followed.

弁19a,19bの開閉速度は、弁19a,1
9bの開閉時に生じる再生ガスの圧力変動を圧力
調節計24で検出でき、かつ、圧力調節計24で
圧力調節弁26を閉止方向並びに開放方向に操作
できるような速度に、弁19a,19bに供給さ
れる気体の流量を流量調節弁30a〜30dで緩
やかに減量並びに増量させることで調節される。
The opening/closing speed of the valves 19a, 19b is
Supply to the valves 19a and 19b at such a speed that the pressure regulator 24 can detect the pressure fluctuation of the regeneration gas that occurs when opening and closing the regeneration gas 9b, and the pressure regulator 24 can operate the pressure regulating valve 26 in the closing direction and the opening direction. The flow rate of the gas is adjusted by gently decreasing and increasing the flow rate of the gas using the flow control valves 30a to 30d.

本実施例のような吸着装置では、気体が開閉操
作される弁の開閉速度を、再生ガス圧力調節装置
の圧力調節速度が追従できる速度に調節できるの
で、気体で開閉操作される弁の開閉時に生じる再
生ガスの急激な圧力変動を抑制することができ
る。
In the adsorption device of this embodiment, the opening/closing speed of the valve that is opened and closed by gas can be adjusted to a speed that can be followed by the pressure adjustment speed of the regeneration gas pressure regulator. It is possible to suppress rapid pressure fluctuations in the generated regeneration gas.

なお、本実施例では、気体で開閉操作される弁
に複動シリンダ駆動型の弁を用いた場合について
説明したが、この他に、単動シリンダ駆動型の弁
を用いても良い。
In this embodiment, a case has been described in which a double-acting cylinder-driven valve is used as the valve that is opened and closed by gas, but a single-acting cylinder-driven valve may also be used.

本発明は、以上説明したように、気体で開閉操
作される弁の開閉速度を、再生ガス圧力調節装置
の圧力調節速度が追従できる速度に調節可能な流
量調節弁を設けたということで、気体で開閉操作
される弁の開閉時に生じる再生ガスの急激な圧力
変動を抑制できるので、吸着装置を安定して運転
できる効果がある。
As explained above, the present invention provides a flow rate regulating valve that can adjust the opening/closing speed of a valve that is operated by gas to a speed that can be followed by the pressure regulating speed of the regeneration gas pressure regulating device. Since the rapid pressure fluctuation of the regeneration gas that occurs when the valve is opened and closed can be suppressed, the adsorption device can be operated stably.

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

第1図は、従来の吸着装置の系統図、第2図
は、本発明による吸着装置の一実施例を示す系統
図である。 10a,10b……吸着塔、19a,19b…
…弁、21a,21b,22cから22f,25
……導管、24……圧力調節計、26……圧力調
節弁、30aから30d……流量調節弁。
FIG. 1 is a system diagram of a conventional adsorption device, and FIG. 2 is a system diagram showing an embodiment of the adsorption device according to the present invention. 10a, 10b...adsorption tower, 19a, 19b...
...Valves, 21a, 21b, 22c to 22f, 25
... conduit, 24 ... pressure regulator, 26 ... pressure control valve, 30a to 30d ... flow control valve.

Claims (1)

【特許請求の範囲】[Claims] 1 再生ガスで再生される吸着塔と、気体で開閉
操作され前記吸着塔への前記再生ガスの供給、停
止を行う弁と、前記吸着塔へ供給される前記再生
ガスの圧力を検出する圧力調節計と、該圧力調節
計からの指令により前記再生ガスで前記吸着塔へ
の供給前に放出される再生ガスの量を調節する圧
力調節弁と、前記弁の開閉時に前記圧力調節弁の
開閉方向操作速度が追従可能な速度に前記弁の開
閉速度を調節する前記気体の流量調節弁とを具備
したことを特徴とする吸着装置。
1. An adsorption tower that is regenerated with regeneration gas, a valve that is opened and closed by gas to supply and stop the regeneration gas to the adsorption tower, and a pressure regulator that detects the pressure of the regeneration gas that is supplied to the adsorption tower. a pressure regulating valve that adjusts the amount of regeneration gas released before the regeneration gas is supplied to the adsorption tower according to a command from the pressure regulator; and an opening/closing direction of the pressure regulating valve when the valve is opened or closed. An adsorption device comprising: a gas flow rate control valve that adjusts the opening/closing speed of the valve to a speed that can be followed by an operating speed.
JP57061061A 1982-04-14 1982-04-14 Adsorption device Granted JPS58178181A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57061061A JPS58178181A (en) 1982-04-14 1982-04-14 Adsorption device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57061061A JPS58178181A (en) 1982-04-14 1982-04-14 Adsorption device

Publications (2)

Publication Number Publication Date
JPS58178181A JPS58178181A (en) 1983-10-19
JPS625007B2 true JPS625007B2 (en) 1987-02-03

Family

ID=13160273

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57061061A Granted JPS58178181A (en) 1982-04-14 1982-04-14 Adsorption device

Country Status (1)

Country Link
JP (1) JPS58178181A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60194273A (en) * 1984-03-14 1985-10-02 株式会社日立製作所 Air separation equipment pressure control device

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5180682A (en) * 1975-01-13 1976-07-14 Toray Industries Kongogasuno bunrihoho

Also Published As

Publication number Publication date
JPS58178181A (en) 1983-10-19

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