JPS5822690B2 - Pressure monitoring and operating device for vacuum equipment - Google Patents

Pressure monitoring and operating device for vacuum equipment

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Publication number
JPS5822690B2
JPS5822690B2 JP53011444A JP1144478A JPS5822690B2 JP S5822690 B2 JPS5822690 B2 JP S5822690B2 JP 53011444 A JP53011444 A JP 53011444A JP 1144478 A JP1144478 A JP 1144478A JP S5822690 B2 JPS5822690 B2 JP S5822690B2
Authority
JP
Japan
Prior art keywords
pressure
protection unit
differential pressure
normal
vacuum
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
JP53011444A
Other languages
Japanese (ja)
Other versions
JPS54104885A (en
Inventor
鈴木勝美
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 JP53011444A priority Critical patent/JPS5822690B2/en
Publication of JPS54104885A publication Critical patent/JPS54104885A/en
Publication of JPS5822690B2 publication Critical patent/JPS5822690B2/en
Expired legal-status Critical Current

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  • Measuring Fluid Pressure (AREA)
  • Testing Of Devices, Machine Parts, Or Other Structures Thereof (AREA)
  • Examining Or Testing Airtightness (AREA)

Description

【発明の詳細な説明】 本発明は真空装置の圧力を監視制御する圧力監視操作装
置に係り、特に圧力上昇による真空機器の破損を防止す
るために好適な圧力異常状態を検出、しゃ断、排気を行
しめるための真空装置用の圧力監視操作装置に関するも
のである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a pressure monitoring and operating device that monitors and controls the pressure of a vacuum device, and in particular detects, shuts off, and exhausts abnormal pressure conditions suitable for preventing damage to vacuum devices due to pressure rise. The present invention relates to a pressure monitoring and operating device for a vacuum device for operating a vacuum device.

真空装置において、装置の一部が破断して外気流体が洩
れ込んだ際の、検出・しゃ断・排気を行う場合に、従来
は以下に示すような手段を用いていた。
BACKGROUND ART Conventionally, in a vacuum device, when a part of the device breaks and outside air fluid leaks, the following means have been used to detect, shut off, and exhaust the air.

第1図において、図示されてない複数の真空機器および
配管とから構成されている防護単位1゜2.3と、この
防護単位間を接続するプロセス配W6L62、とこのプ
ロセス配管に設置したしゃ新井12,13、の間で通常
のプロセス流体が処理されている。
In Figure 1, a protection unit 1゜2.3 consisting of a plurality of vacuum equipment and piping (not shown), a process wiring W6L62 that connects this protection unit, and a shield installed in this process piping are shown. 12 and 13, normal process fluids are being processed.

防護単位1,2,3にはそれぞれ通常排気弁21.22
,23、および緊急排気弁31,32,33、が接続さ
れており、上記弁21.22,23,31,32,33
、は正常運転状態では閉じている。
Protection units 1, 2 and 3 each have a normal exhaust valve 21.22
, 23, and emergency exhaust valves 31, 32, 33 are connected to the valves 21, 22, 23, 31, 32, 33.
, is closed under normal operating conditions.

この状態で例えば防御単位2の1部が破断して、外気流
体が洩れこんだ際の圧力変化は第2図のようになる。
In this state, for example, when a part of the protection unit 2 breaks and outside air fluid leaks in, the pressure change will be as shown in FIG. 2.

すなわち時刻toまでは正常に運転されており、時刻t
In other words, it is operating normally until time to, and until time t
.

にて防護単位2の一部が破断したとする。Suppose that a part of protection unit 2 breaks at .

このとき各防護単位の圧力は次第に上昇するが、その上
昇速度は破断した位置や、破断の大きさによって異なり
、まだ防護単位内の配管、機器の時間遅れの差異により
破断した防護単位2の圧力計72の圧力が必ずしも最初
に上昇するとは限らないために、まず、圧力計71,7
2,73、のうちいずれかがレベル高となったとき(す
なわち時刻tt)c第1図のしゃ新井12,13.を閉
じてすべての防護単位1,2,3−を隔離する。
At this time, the pressure in each protection unit gradually increases, but the rate of increase varies depending on the location of the rupture and the size of the rupture. Since the pressure at the pressure gauge 72 does not necessarily rise first, the pressure at the pressure gauges 71 and 7
2, 73, when the level becomes high (that is, at time tt). Close and isolate all protection units 1, 2, 3-.

この状態では、正常な防護単位1,3の中へ洩れ込む外
気の流体は皆無であるから圧力計71,73の指示は各
々独立な防護単位1,3の平衝状態に向ってゆるやかに
変化をするのみである。
In this state, there is no outside air fluid leaking into the normal protection units 1 and 3, so the indications on the pressure gauges 71 and 73 gradually change toward the equilibrium state of the independent protection units 1 and 3. It only does this.

一方破断した防護単位2のなかへU外気が洩れ込んで来
るため、更に急激な圧力上昇を示し、レベル高嵩となる
On the other hand, since the outside air leaks into the broken protection unit 2, the pressure increases even more rapidly and the level increases.

この時刻t2の時点で防護単位2を破断したことを知り
以下第1図に示した緊急排気用弁32、を開けることに
より破断した防護単位2のみを緊急排気装置30により
排気し、正常な防護単位1,3を通常排気装置20によ
り排気することにより、破断した防護単位のプロセス流
体が外気へ流出することを防ぎ、また正常な防御単位内
の真空機器が圧力上昇により破損することを防いでいる
At this time t2, it is learned that the protective unit 2 has been ruptured, and by opening the emergency exhaust valve 32 shown in FIG. By evacuating the units 1 and 3 using the normal exhaust device 20, the process fluid in the ruptured protection unit is prevented from flowing out to the outside air, and the vacuum equipment in the normal protection unit is also prevented from being damaged due to the pressure increase. There is.

しかし、この方法の欠点としては (1)防護単位内の真空機器の耐圧限界(上限)および
耐持続時間が比較的低いために、第2図に示すレベル高
嵩の設定値を大きくできない。
However, the drawbacks of this method are (1) the pressure limit (upper limit) and the durability time of the vacuum equipment within the protection unit are relatively low; therefore, the set value of the level height shown in FIG. 2 cannot be increased;

(2)シたがって破断した位置および、大きざによjつ
では正常な防護単位の圧力が最初にレベル高嵩に達する
ために、例えば、正常な防護単位1を緊急排気装置30
.で排気し、正常な防護単位3と破断した防護単位2を
ともに通常排気装置20で排気することになる。
(2) Therefore, depending on the location and size of the rupture, the pressure of the normal protection unit reaches a high level first, so that, for example, the normal protection unit 1 is removed from the emergency exhaust system 30.
.. Both the normal protection unit 3 and the broken protection unit 2 are evacuated by the normal exhaust device 20.

この場合には防。護単位2から防護単位3へ外気が逆流
し、防護単位3の正常な機器を破損させることになる。
Prevention in this case. Outside air will flow back from protection unit 2 to protection unit 3, damaging normal equipment in protection unit 3.

本発明の目的は、上記した従来技術の欠点をなくし、異
常が生じた真空機器を早期にしゃ断隔離して異常が生じ
た真空機器からのガス排出を円滑〉に行い真空機器の破
損を防止することにある。
The purpose of the present invention is to eliminate the above-mentioned drawbacks of the prior art, to quickly shut off and isolate a vacuum device in which an abnormality has occurred, and to smoothly discharge gas from the vacuum device in which an abnormality has occurred, thereby preventing damage to the vacuum device. There is a particular thing.

本発明は防護単位毎に圧力を検知する圧力計としゃ新井
の両端圧力差を検知する差圧計の出力信号により圧力異
常個所を検出、該当せるしゃ新井を閉”とすることによ
り異常防護単位を隔離し5更に緊急および通常の2通り
の排気操作を行い正常防護単位機器の破損に至る事故波
及を防止することを可能としたものである。
The present invention detects abnormal pressure points using the output signals of the pressure gauge that detects the pressure for each protection unit and the differential pressure gauge that detects the pressure difference between both ends of the shield well, and closes the corresponding shield well, thereby identifying the abnormal protection unit. This makes it possible to isolate the equipment and perform two types of exhaust operations, emergency and normal, to prevent accidents from spreading that could lead to damage to normally protected unit equipment.

本発明の実施例を第3図により説明する。An embodiment of the present invention will be explained with reference to FIG.

第3図において図示されていない複数の真空機J器およ
び配管より構成される防護単位1,2,3はプロセス配
管61,62に接続されている。
Protection units 1, 2, and 3, which are composed of a plurality of vacuum machines and piping (not shown in FIG. 3), are connected to process piping 61, 62.

このプロセス配管にはしゃ新井12,13が設置されて
おり異常時[i”閉″することにより各々の防護単位は
隔離される。
A shield well 12, 13 is installed in this process piping, and when an abnormality occurs [i"closed", each protection unit is isolated.

各々防護単位には緊急排気配管51,52゜53および
緊急排気弁31,32,33を介し緊急排気ヘッダー5
4を経由し緊急排気装置30へ接続されている。
Each protection unit is connected to an emergency exhaust header 5 via emergency exhaust pipes 51, 52, 53 and emergency exhaust valves 31, 32, 33.
4 to the emergency exhaust system 30.

また各々防護単位には通常排気配管41,42.。In addition, each protection unit has normal exhaust piping 41, 42. .

43および通常排気ヘッダー44を経由し通常排気装置
20へ接続されている。
43 and a normal exhaust header 44 to the normal exhaust device 20.

緊急排気弁31゜32.33、は異常防護単位のみ゛開
″となり正常防護単位は閉となっている。
The emergency exhaust valves 31, 32, and 33 are "open" only for the abnormal protection unit and closed for the normal protection unit.

通常排気弁21゜22.23は正常防護単位のみパ開″
となり異常防護単位ハ゛閉″となっている。
Normal exhaust valves 21゜22.23 are open only for normal protection units.''
Therefore, the abnormality protection unit is "highly closed".

通常の運転時はしゃ新井12,13、を除いては全て゛
閉″状態になっている。
During normal operation, all of the wells except for the shield wells 12 and 13 are in a "closed" state.

確実に圧力異常個所を検出するために、従来性われてい
る圧力計のほかに、しゃ新井12および13の両端の圧
力差を検出するための差圧計81゜82を設置した。
In order to reliably detect pressure abnormalities, in addition to conventional pressure gauges, differential pressure gauges 81 and 82 were installed to detect the pressure difference between both ends of the shield wells 12 and 13.

次に本発明の圧力監視操作装置の動作について第4図に
示す、ブロック図により説明する。
Next, the operation of the pressure monitoring and operating device of the present invention will be explained with reference to the block diagram shown in FIG.

■ 圧力異常個所の検出方式 圧力異常個所の検出は差圧計81,82により行う。■ Detection method for abnormal pressure points Detection of pressure abnormalities is performed using differential pressure gauges 81 and 82.

差圧計81はしゃ新井12、の両端のP、−P2点間の
圧力差を検知しその値が規定値を起えたときに出力信号
が表われる。
The differential pressure gauge 81 detects the pressure difference between two points P and -P at both ends of the pressure gauge 12, and when the value reaches a specified value, an output signal appears.

防護単位1または2の一部が破断した場合には外気の洩
れ込みにより破断防護単位の圧力が上昇する。
When a part of the protection unit 1 or 2 breaks, the pressure of the broken protection unit increases due to leakage of outside air.

しゃ新井の両端のPI F2間の圧力差は大きくなる
The pressure difference between PIF2 at both ends of the shiarai increases.

もう一方の差圧計82が圧力差測定しようとするp3−
p、間に差圧が表われるか、否かによって防護単位1ま
た2かのどちらが破断事故を起しているかを判定するも
のである。
p3- where the other differential pressure gauge 82 attempts to measure the pressure difference
It is determined whether the protection unit 1 or 2 has caused a breakage accident, depending on whether or not a differential pressure appears between the protection units 1 and 2.

すなわち差圧計81が、″差圧あす″を経出し、差圧計
82が差圧を検出しておれば、A3のANDが成立し防
護単位2に破断事故が起ったと判定ししゃ新井12,1
3、を閉”にし防護単位を夫々隔離する。
In other words, if the differential pressure gauge 81 indicates "differential pressure tomorrow" and the differential pressure gauge 82 detects the differential pressure, the AND of A3 is established and it is determined that a rupture accident has occurred in the protection unit 2. 1
3. Close and isolate each protection unit.

また差圧計82が差圧を検出してないときにばN2のN
OT回路の出力がありとなりA1のANDが成立し防護
単位1に破断事故が起ったと判定し、しゃ断12を閉と
し防護単位1を隔離する。
Also, if the differential pressure gauge 82 is not detecting differential pressure, the N2
The output of the OT circuit is present, the AND of A1 is established, it is determined that a breakage accident has occurred in the protection unit 1, the breaker 12 is closed, and the protection unit 1 is isolated.

差圧計82が差圧ありを検出し差圧計81が差圧ありを
検出しない場合はN1のNOT回路の出力がありとなり
A2のANDが成立し防護単位3に破断事故が起ったと
判定ししゃ新井13を閉とし防護単位3を隔離する。
If the differential pressure gauge 82 detects that there is a differential pressure and the differential pressure gauge 81 does not detect that there is a differential pressure, the output of the NOT circuit of N1 is present, the AND of A2 is established, and it is determined that a rupture accident has occurred in the protection unit 3. Arai 13 is closed and protection unit 3 is isolated.

■ 緊急排気と通常排気の判別 防護単位2に破断事故が起った場合、前記■にてしゃ新
井12,13.をパ閉”としたため外気の洩れ込みによ
りに更に圧力は上昇する。
■ Distinguishing between emergency exhaust and normal exhaust If a breakage accident occurs in protection unit 2, Arai 12, 13. Since the valve was closed, the pressure rose further due to the leakage of outside air.

防護単位2の圧力計72の圧力高″を検出、他の防護単
位1,3の圧力計71,73が圧力高′″を検出してな
いことを条件にA5のANDが成立して緊急排気弁32
を゛開″正常防護単位1,3の通常排気弁21,23を
°゛開″し排気操作を行う。
Detecting the high pressure of the pressure gauge 72 of protection unit 2, and assuming that the pressure gauges 71 and 73 of other protection units 1 and 3 do not detect the high pressure, AND of A5 is established and emergency evacuation is performed. valve 32
The normal exhaust valves 21 and 23 of the normal protection units 1 and 3 are opened and the exhaust operation is performed.

すなわち排気系ライン経由異常防護単位より正常防護単
位への逆流を防止するために圧力計の出力条件を比較し
排気弁を開放Iト気操作を行う。
That is, in order to prevent backflow from the abnormal protection unit to the normal protection unit via the exhaust system line, the output conditions of the pressure gauges are compared and the exhaust valve is opened.

したがって従来方式の逆流による正常防護単位機器の破
損事故を確実に防止可能となる。
Therefore, it is possible to reliably prevent damage to normally protected unit equipment due to backflow in the conventional method.

防護単位1が破断事故時には圧力計71が圧パ高″を検
出し圧力計72.73が圧力高を検出してないことを条
件にまた防護単位3が破断事故時には圧力計73が圧力
高を検出、圧力計7L72が圧力高を検出してないこと
を条件に対応ぜる緊急排気弁および通常排気弁をパ開放
″シて排気操作を行うようにする。
If the protection unit 1 ruptures, the pressure gauge 71 detects a high pressure, and the pressure gauges 72 and 73 do not detect a high pressure.If the protection unit 3 ruptures, the pressure gauge 73 detects a high pressure. When the pressure gauge 7L72 detects no high pressure, the corresponding emergency exhaust valve and normal exhaust valve are opened and the exhaust operation is performed.

上述の如く本発明の実施例によれば防護単位の一部破断
事故時にも確実に事故防護単位を隔離し、異常防護単位
を緊急、正常防護単位を通常排気操作を行うことにより
、事故範囲を極小化するとともに正常防護栄位への波及
を防止することが可能となる。
As described above, according to the embodiment of the present invention, even in the event of an accident in which a part of the protection unit breaks, the accident protection unit is reliably isolated, and the abnormal protection unit is operated in an emergency manner, and the normal protection unit is normally exhausted, thereby reducing the area of the accident. This makes it possible to minimize the damage and prevent it from spreading to the normal protective status.

本発明によれば、差王計の出力信号を用いてしゃ断弁を
操作しているので、異常の生じた真空機器を短時間に隔
離でき、異常の生じた真空機器から正常な真空機器への
外気の流入を最小限に抑制できる。
According to the present invention, since the output signal of the difference meter is used to operate the shutoff valve, it is possible to isolate the abnormal vacuum equipment in a short time, and to switch from the abnormal vacuum equipment to the normal vacuum equipment. The inflow of outside air can be minimized.

寸た、異常の生じた真空機器の排気を緊急排気装置に切
換えて行うので、IE常な真空機器から排出されるガス
と異常が生じた真空機器から排気されるガスの混入を防
止できる。
Since the vacuum equipment in which the abnormality has occurred is immediately switched to the emergency exhaust system, it is possible to prevent the gas exhausted from the normal vacuum equipment from mixing with the gas exhausted from the abnormal vacuum equipment.

異常が生じた真空機器を短時間に隔離できてその真空機
器からのガスの排気を通常排気装置から緊急排気装置に
切換えるので、真空機器の破損を防IL、できる。
Vacuum equipment in which an abnormality has occurred can be isolated in a short time, and gas exhaust from the vacuum equipment can be switched from a normal exhaust system to an emergency exhaust system, so damage to the vacuum equipment can be prevented.

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

第1図に従来例の系統図、第2図に従来例における圧力
変化を示す特性図−第3図は本発明の一実施例を示す系
統図であり、第4図は本発明の圧力監視操作装置の動作
ブロック図である。 1.2,3・・・防護単位、12,13・・・しゃ断弁
、20・・・通常排気装置、21,22,23・・・通
常排気弁、30・・・緊急排気装置、31,32,33
・・・緊急排気用弁、41,42,43・・・通常排気
配管、44・・・通常排気ヘッダー、51,52,53
・・・緊急排気配管、54・・・緊會誹気ヘッダー、6
1゜62・・・プロセス配管、71 .72,73・・
・圧力計、8L81差圧計。
Fig. 1 is a system diagram of the conventional example, Fig. 2 is a characteristic diagram showing pressure changes in the conventional example, Fig. 3 is a system diagram showing an embodiment of the present invention, and Fig. 4 is a pressure monitoring system of the present invention. FIG. 3 is an operational block diagram of the operating device. 1.2,3...Protection unit, 12,13...Shutoff valve, 20...Normal exhaust system, 21,22,23...Normal exhaust valve, 30...Emergency exhaust system, 31, 32, 33
...Emergency exhaust valve, 41, 42, 43... Normal exhaust piping, 44... Normal exhaust header, 51, 52, 53
...Emergency exhaust piping, 54...Emergency air header, 6
1゜62...process piping, 71. 72, 73...
・Pressure gauge, 8L81 differential pressure gauge.

Claims (1)

【特許請求の範囲】[Claims] 1 複数の真空機器、前記真空機器間を連絡する配管お
よびこの配管に設けられたしゃ新井を有する真空装置の
圧力監視操作装置において各々のしゃ新井の両端の差圧
を測定する複数の差圧計を前記配管にそれぞれ取付け、
各々の真空機器に圧力計を設け、前記差圧計にて差圧が
検出された時にその差圧を検出した前記差圧計が設けら
れている前記配管に取付けられたしゃ新井を閉鎖する第
1の制御手段を有し、前記圧力計の出力である圧力信号
が設定値を越えしかも前記差圧計の出力である差圧信号
が入力された時に前記圧力信号が設定値を越えた真空機
器からのガス排気を、通常排気装置から緊急排気装置に
切換える第2の制御手段を有することを特徴とする真空
装置の圧力監視操作装置。
1. In a pressure monitoring and operating device for a vacuum device that has a plurality of vacuum devices, piping that connects the vacuum devices, and a strain relief well provided in this piping, a plurality of differential pressure gauges are installed to measure the differential pressure between both ends of each strain relief well. Attach each to the above piping,
Each vacuum device is provided with a pressure gauge, and when the differential pressure is detected by the differential pressure gauge, a first valve is installed to close the arai, which is attached to the piping in which the differential pressure gauge is installed. Gas from a vacuum device having a control means, in which the pressure signal output from the pressure gauge exceeds the set value and when the differential pressure signal output from the differential pressure gauge is input, the pressure signal exceeds the set value. A pressure monitoring and operating device for a vacuum device, comprising a second control means for switching exhaust from a normal exhaust system to an emergency exhaust system.
JP53011444A 1978-02-06 1978-02-06 Pressure monitoring and operating device for vacuum equipment Expired JPS5822690B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP53011444A JPS5822690B2 (en) 1978-02-06 1978-02-06 Pressure monitoring and operating device for vacuum equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP53011444A JPS5822690B2 (en) 1978-02-06 1978-02-06 Pressure monitoring and operating device for vacuum equipment

Publications (2)

Publication Number Publication Date
JPS54104885A JPS54104885A (en) 1979-08-17
JPS5822690B2 true JPS5822690B2 (en) 1983-05-10

Family

ID=11778255

Family Applications (1)

Application Number Title Priority Date Filing Date
JP53011444A Expired JPS5822690B2 (en) 1978-02-06 1978-02-06 Pressure monitoring and operating device for vacuum equipment

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Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02289184A (en) * 1989-04-26 1990-11-29 Unitika Ltd Deodorizing textile product
JPH02289185A (en) * 1989-04-26 1990-11-29 Unitika Ltd Production of deodorizing textile product

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5299877A (en) * 1976-02-18 1977-08-22 Nippon Kokan Kk Detector for damage and leakage of pipeline

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5299877A (en) * 1976-02-18 1977-08-22 Nippon Kokan Kk Detector for damage and leakage of pipeline

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JPS54104885A (en) 1979-08-17

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