JPH0719548Y2 - Pressure swing type mixed gas separator - Google Patents

Pressure swing type mixed gas separator

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Publication number
JPH0719548Y2
JPH0719548Y2 JP1162990U JP1162990U JPH0719548Y2 JP H0719548 Y2 JPH0719548 Y2 JP H0719548Y2 JP 1162990 U JP1162990 U JP 1162990U JP 1162990 U JP1162990 U JP 1162990U JP H0719548 Y2 JPH0719548 Y2 JP H0719548Y2
Authority
JP
Japan
Prior art keywords
gas
abnormality
pressure
mixed gas
throttle 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.)
Expired - Lifetime
Application number
JP1162990U
Other languages
Japanese (ja)
Other versions
JPH03102218U (en
Inventor
直樹 岡島
典男 国保
Original Assignee
シーケーデイ株式会社
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 シーケーデイ株式会社 filed Critical シーケーデイ株式会社
Priority to JP1162990U priority Critical patent/JPH0719548Y2/en
Publication of JPH03102218U publication Critical patent/JPH03102218U/ja
Application granted granted Critical
Publication of JPH0719548Y2 publication Critical patent/JPH0719548Y2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Drying Of Gases (AREA)
  • Separation Of Gases By Adsorption (AREA)

Description

【考案の詳細な説明】 産業上の利用分野 本考案は分離剤を充填した2本の分離筒で混合ガス中の
1種または2種以上のガスを分離する分離行程と分離済
みのガスの一部を利用して分離剤からガスを取り去る再
生行程とを交互に行うようにした圧力スウイング式混合
ガス分離装置に関し、特に、流入ガス量または吐出ガス
量と流入ガスの圧力及び温度に応じて効率の良い自動運
転を行うようにした装置に関する。
DETAILED DESCRIPTION OF THE INVENTION Industrial Field of the Invention The present invention relates to a separation process for separating one or more kinds of gas in a mixed gas by two separation cylinders filled with a separating agent, and a separated gas. Pressure swing-type mixed gas separation device in which a regeneration process for removing gas from a separating agent is alternately performed by using a section, and in particular, the efficiency depends on the amount of inflow gas or discharge gas and the pressure and temperature of the inflow gas. The present invention relates to a device for performing good automatic driving.

従来の技術及び考案が解決しようとする課題 上記のような圧力スウイング式混合ガス分離装置におい
ては、再生行程に用いる分離済みのガスの量を必要最少
限にするのが最も効率の良い運転方法である。そこで、
近年このような混合ガス分離装置においては、再生用ガ
スの流通路に可変絞り弁を介設するとともに、流入口側
の未処理の混合ガスの圧力及び温度とその未処理の混合
ガスまたは吐出口側の処理済みガスの流量を検出するセ
ンサを設け、各センサで検出した圧力、温度及び流量を
デイジタル化してマイクロコンピユータに入力し、その
ROM(リードオンリメモリ)に格納されたプログラムに
従つてCPU(中央処理装置)で演算が行われ、その出力
信号により可変絞り弁の開度を制御するようにしたもの
が普及しつつある。しかるに、流量センサ、温度センサ
または圧力センサに異常が生じて誤つた検出値がマイク
ロコンピユータに入力されると可変絞り弁の適正な制御
が不能となり、特に、可変絞り弁の開度が適正値より小
さい方向に誤つて制御された場合には、再生に供される
処理済みガスの量が不足し、再生が不十分なまま分離行
程に移るため、分離が不十分なガスが吐出されるばかり
でなく、このような運転が継続されると分離剤に過剰な
ガスが吸着または吸収されて再生不能となり、高価な分
離剤が無駄になるおそれがあつた。
In the pressure swing type mixed gas separation device as described above, it is the most efficient operation method to minimize the amount of separated gas used in the regeneration process. is there. Therefore,
In recent years, in such a mixed gas separation device, a variable throttle valve is provided in the flow path of the regenerating gas, and the pressure and temperature of the untreated mixed gas on the inlet side and the untreated mixed gas or discharge port. A sensor for detecting the flow rate of the processed gas on the side is provided, and the pressure, temperature, and flow rate detected by each sensor are digitalized and input to the micro computer.
It is becoming popular that a CPU (Central Processing Unit) performs an operation according to a program stored in a ROM (Read Only Memory) and the output signal thereof controls the opening of a variable throttle valve. However, if an incorrect detection value is input to the microcomputer due to an abnormality in the flow rate sensor, temperature sensor, or pressure sensor, the variable throttle valve cannot be controlled properly. If it is erroneously controlled in a small direction, the amount of treated gas used for regeneration will be insufficient, and the process will move to the separation process with insufficient regeneration, so that only insufficiently discharged gas will be discharged. However, if such an operation is continued, excess gas is adsorbed or absorbed by the separating agent and regeneration cannot be performed, and the expensive separating agent may be wasted.

課題を解決するための手段 本考案はこのような課題を解決するための手段として、
第1図に示すように、各センサの検出値があらかじめ設
定された範囲外となった場合に異常を検知する異常検知
手段と、その異常検知手段が異常を検知したときに可変
絞り弁を開方向へ制御する制御手段と、異常を表示する
異常表示手段を設けた構成とした。
Means for Solving the Problems The present invention is, as means for solving such problems,
As shown in FIG. 1, an abnormality detecting means for detecting an abnormality when the detection value of each sensor is out of a preset range, and a variable throttle valve is opened when the abnormality detecting means detects the abnormality. The control means for controlling the direction and the abnormality display means for displaying the abnormality are provided.

作用及び効果 本考案は上記構成になり、各センサが異常を生ずると、
可変絞り弁が開方向に制御されて再生用の処理済みガス
の量が増大するから、運転効率は低下するものの、分離
度の低いガスが吐出されたり、分離剤が再生不要になつ
たりする事態が回避されるとともに、異常の発生が表示
されるから、通時に異常の生じたセンサを交換して正常
な経済運転へ移行することができる効果がある。
Function and effect The present invention has the above-mentioned configuration, and when each sensor has an abnormality,
The variable throttle valve is controlled in the opening direction to increase the amount of treated gas for regeneration, which reduces operating efficiency, but discharges a gas with a low degree of separation or causes the separation agent to become unnecessary for regeneration. Since the occurrence of the abnormality is displayed and the occurrence of the abnormality is displayed, it is possible to replace the sensor in which the abnormality has occurred at the time of communication and to shift to normal economic operation.

実施例 以下、本考案を加圧空気の除湿装置に適用した一実施例
を添付図面に基づいて説明する。
Embodiment An embodiment in which the present invention is applied to a dehumidifying device for pressurized air will be described below with reference to the accompanying drawings.

第2図は本実施例の全体構成を示し、流入口9から流入
した高圧多湿の未処理空気は開閉弁1a、2aの開弁により
シリカゲル等の吸着剤が充填された第1分離筒6a内を通
過する際に水蒸気が吸着剤に吸着して分離され、乾燥し
た空気は吐出口8から吐出されるとともに、開閉弁4bの
開弁により第2分離筒6bが排出口7から大気に連通して
いて、第1分離筒6aから吐出された低湿度の空気の一部
が可変絞り弁13を通つて急膨張することによりさらに低
湿度となつて第2分離筒6b内に流入し、前行程の吸着行
程において吸着した水分を吸着剤から奪つて乾燥させる
ことにより再生させ、排出口7から排出される。一定時
間が経過すると開閉弁4bが閉じて開閉弁3bが開くことに
より処理済みの高圧空気が第2分離筒6b内に充填されて
昇圧し、ついで、開閉弁1a、2aが閉じて開閉弁4aが開く
ことにより第1分離筒6a内に残留していた高圧空気が排
出口7から排出されるとともに、開閉弁1b、2bが開いて
未処理の高圧空気が第2分離筒6bに流入し、再生された
吸着剤に水蒸気が吸着されて乾燥した空気が吐出口8か
ら吐出され、乾燥空気の一部は可変絞り弁13を通つて膨
張することによりさらに乾燥して第1分離筒6a内に流入
し、その中の吸着剤から水分を奪つて乾燥させ、再生さ
せる。このように、吸着と再生の行程を第1分離筒6aと
第2分離筒6bとにおいて交互に行うことにより多湿の空
気から水分を除去した乾燥空気を連続して得ることがで
きる。なお、5a、5bはドレンコツク、10はドレン排出口
である。
FIG. 2 shows the overall configuration of this embodiment. The high-pressure and high-humidity untreated air flowing in from the inlet 9 is in the first separation cylinder 6a filled with an adsorbent such as silica gel by opening the opening / closing valves 1a and 2a. Water vapor is adsorbed and separated by the adsorbent when passing through the air, and the dry air is discharged from the discharge port 8 and the second separation cylinder 6b communicates with the atmosphere from the discharge port 7 by opening the open / close valve 4b. However, a part of the low-humidity air discharged from the first separation cylinder 6a rapidly expands through the variable throttle valve 13 to become further low humidity, and then flows into the second separation cylinder 6b. In the adsorption process, the adsorbed water is taken from the adsorbent and dried to be regenerated and discharged from the discharge port 7. After a certain period of time, the open / close valve 4b is closed and the open / close valve 3b is opened, so that the treated high-pressure air is filled in the second separation cylinder 6b to increase the pressure, and then the open / close valves 1a and 2a are closed to open / close the open / close valve 4a. Is opened, the high pressure air remaining in the first separation cylinder 6a is discharged from the outlet 7, the open / close valves 1b and 2b are opened, and unprocessed high pressure air flows into the second separation cylinder 6b. Water that has been adsorbed by the regenerated adsorbent and dried air is discharged from the discharge port 8, and a part of the dried air is further expanded by passing through the variable throttle valve 13 and further dried, and then dried in the first separation cylinder 6a. It flows in, removes water from the adsorbent in it, dries it, and regenerates it. In this way, by alternately performing the adsorption and regeneration processes in the first separation cylinder 6a and the second separation cylinder 6b, it is possible to continuously obtain dry air from which moisture has been removed from humid air. In addition, 5a and 5b are drain cocks, and 10 is a drain discharge port.

また、未処理空気の流入口9に圧力センサ15と温度セン
サ16が、吐出口8には流量センサ17が夫々取り付けられ
て、アナログ/デイジタル変換回路18を介してマイクロ
コンピュータ19に入力するように接続されており、マイ
クロコンピュータ19の出力部は可変絞り弁13の制御部に
接続されている。
Further, a pressure sensor 15 and a temperature sensor 16 are attached to the inflow port 9 for the untreated air, and a flow rate sensor 17 is attached to the discharge port 8 so that they are input to the microcomputer 19 via the analog / digital conversion circuit 18. The output part of the microcomputer 19 is connected to the control part of the variable throttle valve 13.

以上に説明したところは従来公知の圧力スウイング式除
湿装置にあつて、圧力センサ15、温度センサ16及び流量
センサ17の検出値はデイジタル化されてマイクロコンピ
ュータ19のCPUに入力され、ROMに格納されているプログ
ラムに従つて演算が行われて、制御データに変換され、
その結果が出力部から可変絞り弁13の制御部に入力され
てその開度が制御されるようになつている。上記プログ
ラムの詳細な説明は省略するが、流量は多い程、入気温
度は高い程、また、入気圧力は低い程多量の再生用空気
が必要となるのであつて、これらの場合に可変絞り弁13
の開度が大きくなるように制御されるようになつてい
る。
As described above, in the conventionally known pressure swing type dehumidifier, the detection values of the pressure sensor 15, the temperature sensor 16 and the flow rate sensor 17 are digitalized and input to the CPU of the microcomputer 19, and stored in the ROM. The calculation is performed according to the program that is converted into control data,
The result is input from the output section to the control section of the variable throttle valve 13 to control the opening thereof. Although a detailed description of the above program is omitted, a larger flow rate, a higher intake air temperature, and a lower intake air pressure require a larger amount of regeneration air. Valve 13
Is controlled so that the opening degree of is increased.

本実施例においてはマイクロコンピユータ19のROMに格
納されているプログラムが第3図にフローチヤートで示
すようになつていて、CPUに入力されたデータが異常か
否かが判別される。データが異常か否かはそれぞれのデ
ータが通常起こり得る値の範囲内にあるか否かによつて
判別されるのであり、その許容範囲は予めROMに入力さ
れている。データに異常がない場合は従来どおり制御デ
ータに変換されて可変絞り弁13の制御部に入力され、効
率の高い運転が継続される。これに対し、データに異常
が生じた場合には安全制御へのデータ変換が行われる。
すなわち、流量は許容範囲の最大値へ、入気温度は許容
範囲の最高値へ、また、入気圧力は許容範囲の最低値に
変換され、これによつて可変絞り弁13は開度が最大とな
るように制御され、効率は低いものの湿度の高い空気が
吐出されたり、吸着剤が再生不能になつたりするのが回
避される。これと同時に異常箇所の判別が行われて警告
ランプ20が点灯され、異常の発生とその箇所が表示され
るようになつている。
In this embodiment, the program stored in the ROM of the microcomputer 19 has a flow chart shown in FIG. 3, and it is determined whether or not the data input to the CPU is abnormal. Whether or not the data is abnormal is determined by whether or not each data is within a range of values that can normally occur, and the allowable range is preliminarily entered in the ROM. When there is no abnormality in the data, the data is converted into control data and input to the control unit of the variable throttle valve 13 as usual, and highly efficient operation is continued. On the other hand, when an abnormality occurs in the data, the data conversion to the safety control is performed.
That is, the flow rate is converted to the maximum value in the allowable range, the intake air temperature is converted to the maximum value in the allowable range, and the intake pressure is converted to the minimum value in the allowable range, whereby the variable throttle valve 13 has the maximum opening degree. Therefore, it is possible to prevent the discharge of high-humidity air having a low efficiency, but the possibility that the adsorbent cannot be regenerated. At the same time, the abnormal portion is discriminated, the warning lamp 20 is turned on, and the occurrence of the abnormality and the portion thereof are displayed.

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

第1図は本考案の構成を示すブロツク図、第2図は本考
案の一実施例の全体構成図、第3図はその制御装置の主
体となるマイクロコンピユータのROMに記載されたプロ
グラムのフローチャートである。 6a、6b:分離筒、8:吐出口、9:流入口、15:圧力センサ、
16:温度センサ、17:流量センサ、19:マイクロコンピユ
ータ、20:警告ランプ
FIG. 1 is a block diagram showing the configuration of the present invention, FIG. 2 is an overall configuration diagram of an embodiment of the present invention, and FIG. 3 is a flow chart of a program written in the ROM of the microcomputer which is the main body of the control device. Is. 6a, 6b: Separation cylinder, 8: Discharge port, 9: Inlet port, 15: Pressure sensor,
16: Temperature sensor, 17: Flow rate sensor, 19: Microcomputer, 20: Warning lamp

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 【請求項1】吸着剤、吸収剤等の分離剤を充填した2本
の分離筒を設け、流入口から流入した未処理の混合ガス
を一方の前記分離筒に高圧で供給して1種または2種以
上のガスを前記分離剤に吸着または吸収させることによ
り分離した処理済みガスを吐出口から吐出する分離行程
と、他方の前記分離筒から吐出される処理済みガスの一
部を可変絞り弁を通すことにより減圧して供給して前記
分離剤に吸着または吸収されていたガスを該分離剤から
取り去つて排気口から排出する再生行程とを、前記2本
の分離筒において一定時間毎に交互に行うようにすると
ともに、前記流入口側の未処理の混合ガスの圧力及び温
度と該未処理の混合ガスまたは前記吐出口側の処理済み
ガスの流量を検出するセンサを各別に設け、該各センサ
の検出値に基づいて前記可変絞り弁の開度を制御して効
率の良い運転を行うようにした圧力スウイング式混合ガ
ス分離装置において、前記各センサの検出値があらかじ
め設定された範囲外となった場合に異常を検知する異常
検知手段と、該異常検知手段が異常を検知したときに前
記可変絞り弁を開方向へ制御する制御手段と、異常を表
示する異常表示手段を設けたことを特徴とする圧力スウ
イング式混合ガス分離装置
1. Two separation cylinders filled with a separating agent such as an adsorbent and an absorbent are provided, and an untreated mixed gas flowing from an inlet is supplied to one of the separation cylinders at a high pressure to obtain one kind or A separation process in which a treated gas separated by adsorbing or absorbing two or more kinds of gases in the separating agent is discharged from a discharge port, and a part of the treated gas discharged from the other separating cylinder is a variable throttle valve. And a regeneration process in which the gas that has been adsorbed or absorbed by the separating agent is removed from the separating agent and is discharged from the exhaust port by reducing the pressure of the gas through the exhaust port. While performing alternately, the pressure and temperature of the untreated mixed gas on the inlet side and sensors for detecting the flow rate of the untreated mixed gas or the treated gas on the outlet side are separately provided, Based on the detection value of each sensor In a pressure swing type mixed gas separation device that controls the opening of the variable throttle valve to perform efficient operation, detects an abnormality when the detection value of each sensor is out of a preset range A pressure slewing type mixing means, which is provided with an abnormality detection means for controlling the variable throttle valve in the opening direction when the abnormality detection means detects an abnormality, and an abnormality display means for displaying the abnormality. Gas separator
JP1162990U 1990-02-08 1990-02-08 Pressure swing type mixed gas separator Expired - Lifetime JPH0719548Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1162990U JPH0719548Y2 (en) 1990-02-08 1990-02-08 Pressure swing type mixed gas separator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1162990U JPH0719548Y2 (en) 1990-02-08 1990-02-08 Pressure swing type mixed gas separator

Publications (2)

Publication Number Publication Date
JPH03102218U JPH03102218U (en) 1991-10-24
JPH0719548Y2 true JPH0719548Y2 (en) 1995-05-10

Family

ID=31515150

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1162990U Expired - Lifetime JPH0719548Y2 (en) 1990-02-08 1990-02-08 Pressure swing type mixed gas separator

Country Status (1)

Country Link
JP (1) JPH0719548Y2 (en)

Also Published As

Publication number Publication date
JPH03102218U (en) 1991-10-24

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