JP2004240840A - Pressure regulator control system - Google Patents

Pressure regulator control system Download PDF

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Publication number
JP2004240840A
JP2004240840A JP2003031009A JP2003031009A JP2004240840A JP 2004240840 A JP2004240840 A JP 2004240840A JP 2003031009 A JP2003031009 A JP 2003031009A JP 2003031009 A JP2003031009 A JP 2003031009A JP 2004240840 A JP2004240840 A JP 2004240840A
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Japan
Prior art keywords
pressure
pressure regulator
governor
degree
deviation
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JP2003031009A
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Japanese (ja)
Inventor
Masayuki Takano
雅之 高野
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Osaka Gas Co Ltd
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Osaka Gas Co Ltd
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Publication date
Application filed by Osaka Gas Co Ltd filed Critical Osaka Gas Co Ltd
Priority to JP2003031009A priority Critical patent/JP2004240840A/en
Publication of JP2004240840A publication Critical patent/JP2004240840A/en
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a pressure regulator control system which performs adjustment so as to maintain correct response to the environment where load or the like is constantly changing. <P>SOLUTION: When the load is small, only a governor 1 is operated. A governor 2 starts to operate when a detecting means 40 detects that a valve-opening reaches 80% which is set as an upper limit of normal operation state. Secondary pressure P2 of the governor 2 is detected by a pressure gauge 62, and degree of deviation of variation from a predefined range is determined by a deviation determination means 63. Speed of response of a servo amplifier 61 is set to a little higher, and a speed modification means 64 reduces it by degrees according to the degree of the deviation. <P>COPYRIGHT: (C)2004,JPO&NCIPI

Description

【0001】
【発明の属する技術分野】
本発明は、流体を輸送する管路系に設けられ、一次圧を二次圧に減圧して流量変動による圧力変動を抑える整圧器の制御状態を、適正な応答性が得られるように調整する整圧器制御システムに関する。
【0002】
【従来の技術】
従来から、都市ガスの供給系統などの流体を輸送する管路系には、負荷に一定の圧力で流体を供給するために、供給される一次圧を減圧し、流量が変動しても二次圧の変動が抑えられるように制御する整圧器が設けられている。整圧器は、ガバナとも呼ばれている。
【0003】
たとえば住宅地に供給する都市ガスでは、炊事や風呂焚きなどが多く行われる時間帯に負荷が大きくなるけれども、他の時間帯には負荷はあまり大きくならない。ピーク時の負荷に対して通常はより小さい負荷となる場合は、複数のガバナを並列に接続して用いることが多い。複数のガバナを並列に接続する多系列ガバナシステムでは、各ガバナ毎に緊急遮断弁が直列に接続される(たとえば、特許文献1参照)。
【0004】
図4は、(a)で多系列ガバナシステムを代表する2系列ガバナシステムの構成を簡略化して示し、(b)でその動作特性を示す。一次管路10から供給される都市ガスなどの流体は、2系列のガバナ11,12で整圧されて二次管路20の負荷に供給される。各ガバナ11,12には緊急遮断弁21,22がそれぞれ接続される。各ガバナ11,12へは、一次管路10から緊急遮断弁21,22を介して一次圧力P1で流体が供給される。2系列ガバナシステム30は、ガバナ11と緊急遮断弁21とを含む第1系列31と、ガバナ12と緊急遮断弁22とを含む第2系列32とからなる。各ガバナ11,12は、一次圧力P1を二次圧力P2付近まで減圧する。すなわちP1>P2である。
【0005】
ガバナ11,12のうちのいずれかに故障などが生じて減圧機能が損なわれると、二次管路20に高い一次圧力P1がかかるおそれがあるので、緊急遮断弁21,22がそれぞれ設けられ、図示は省略しているけれども、それぞれガバナ11,12の二次圧など、動作の異常を検出することによって遮断動作が行われる。故障を生じているガバナを含む系統側の緊急遮断弁が遮断することによって二次管路20の圧力増大を防止する。通常、緊急遮断弁21,22は全開状態となっている。
【0006】
検出手段40は、第1系列31のガバナ11の動作状態として、たとえば弁開度を検出する。第2系列32のガバナ12は、検出手段40が検出する第1系列のガバナ11の弁開度が通常動作状態の上限として設定される値付近にとどまるように動作する。
【0007】
図4(b)は、ガバナ11,12の流量と二次側の圧力との関係を示す。流体の流量は、弁開度にほぼ対応する。各ガバナ11,12は、L11,L12として示すような動作特性を、それぞれ有する。負荷が小さいときは、第1系列31のガバナ11が動作して、第2系列32のガバナ12が待機するように、第2系列32のガバナ12の動作特性L12は、第1系列32のガバナ11の動作特性L11よりも低圧力側で動作するように設定しておく。ただし、第1系列31のガバナ11が弁開度として、たとえば80%を通常動作状態の上限として設定し、ガバナ11が上限付近にとどまるように、第2系列32のガバナ12が稼働を開始する。ガバナ12の設定圧は上昇するように調整され、結果的にL20に示すような動作特性が得られる。
【0008】
第1系列31のガバナ11の弁開度が上限の80%よりも大きくなると、第2系列32のガバナ12の設定圧が上昇するように調整され、ガバナ12の弁開度が大きくなって、流体がガバナ12を介しても負荷に供給される。この結果、第1系列31のガバナ11の弁開度は小さくなり、上限を大きく超えることはないようにすることができる。負荷の減少あるいは第2系列32のガバナ12の稼働で第1系列31のガバナ11の弁開度が上限よりも小さくなると、第2系列32のガバナ12の設定圧は下降し、弁開度は低下する。負荷が第1系列31のガバナ11の弁開度で上限である80%の範囲内であれば、第2系列32のガバナ12は、弁開度が0の全閉状態となる。すなわち、小流量時には、第1系列のガバナ11のみが動作して整圧作用を行う。
【0009】
【特許文献1】
特開平11−282543号公報
【0010】
【発明が解決しようとする課題】
図4(a)に示すような2系列ガバナシステム30では、一方のガバナ11が小流量域から大流量域まで使用され、他方のガバナ12が大流量域で使用される。第2系列32のガバナ12は、第1系列31のガバナ11の弁開度の上限である80%を維持するようにフィードバック制御される。このようなフィードバック制御は、負荷の変動時に過度応答を伴う。
【0011】
すなわち、第1系列31のガバナ11の開度を規定値に保持するように、第2系列32のガバナ12は自らの設定圧を調整しながら制御することになるけれども、この制御はある応答速度で行われる。開度などのフィードバック信号(入力)に対し、速いスピードで対応することができるような出力をコントローラとして機能する検出手段40で発生させれば、俊敏で制度の高い制御が可能になると期待される。しかし、反応を速くしすぎると過応答によるハンチングが生じてしまう。ハンチングが生じると、制御が安定せず、二次圧の変動が継続してしまう。また、ガバナの弁などは、機械的な部分の摺動で摩耗が生じたり、変形の繰返しで疲労が生じたりして、寿命が短くなるおそれがある。このような理由によって、負荷などが刻々と変化する環境では、常に適正な応答性を保つことは困難である。
【0012】
本発明の目的は、負荷などが刻々と変化する環境に対して、適正な応答性を保つように調整することができる整圧器制御システムを提供することである。
【0013】
【課題を解決するための手段】
本発明は、一次側から供給される流体を二次側に減圧して供給し、変動する供給流量に対して予め定める二次圧を保つように制御する整圧器を、適正な応答性が得られるように調整する整圧器制御システムであって、
整圧器の制御動作が反映される指標を検出する指標検出手段と、
指標検出手段によって検出される指標が予め設定される範囲から逸脱する程度を、予め流体の供給流量の変動周期以上に設定される期間内で判定する逸脱判定手段と、
逸脱判定手段の判定する逸脱の程度に応じて、整圧器の制御の応答速度を、該逸脱の程度が予め定める基準の程度に接近する方向に、部分的に変化させる速度変更手段とを含むことを特徴とする整圧器制御システムである。
【0014】
本発明に従えば、整圧器制御システムは、一次側から供給される流体を二次側に減圧して供給し、変動する供給流量に対して予め定める二次圧を保つように制御する整圧器を、適正な応答性が得られるように調整するために、指標検出手段と、逸脱判定手段と、速度変更手段とを含む。指標検出手段は、整圧器の制御動作が反映される指標を検出するので、検出される指標に基づいて、整圧器の制御動作の状態を把握することができる。逸脱判定手段は、指標検出手段によって検出される指標が予め設定される範囲から逸脱する程度を、予め流体の供給流量の変動周期以上に設定される期間内で判定するので、流体供給量の瞬間的な変動の影響を受けないように、指標の変動の設定範囲からの逸脱の程度を判定することができる。速度変更手段は、逸脱判定手段の判定する逸脱の程度に応じて、整圧器の制御の応答速度を、該逸脱の程度が予め定める基準の程度に接近する方向に、部分的に変化させるので、応答速度を少しずつ適正な状態に改善していくことができる。
【0015】
また本発明で、前記整圧器は、複数が同時並行稼働し、
少なくとも1つの整圧器は、他の整圧器の稼働状態が予め定める範囲内となるように二次圧の制御動作を行うことを特徴とする。
【0016】
本発明に従えば、整圧器の応答速度を速くしすぎると、ハンチングを生じ、その結果が他の整圧器に影響し、その整圧器の稼働状態も変動する。この変動は、さらに応答速度の変動を招き、負荷が安定しても2つの整圧器間で一方の開度が大きく他方の開度が小さい状態と、一方の開度が小さく他方の開度が大きい状態とを繰返すような事態になるおそれがある。このような事態では、指標も設定範囲を逸脱しやすくなるので、指標の逸脱を減少させるように応答速度を調整し、適正な制御状態となるようにすることができる。
【0017】
また本発明で、前記指標検出手段は、前記整圧器の少なくとも開度または圧力の一方を前記指標として検出することを特徴とする。
【0018】
本発明に従えば、整圧器の制御動作が反映される指標として、少なくとも開度または圧力を検出する。整圧器が流体の供給流量が変動しても二次圧を一定に保つ制御では弁の開度が変化し、弁の開度を変化させるのは二次圧やパイロット圧などの圧力による。開度は、機械的な変位なので、容易に把握することができる。圧力は管路などから容易に検出することができる。
【0019】
また本発明で、前記整圧器の制御の応答速度は、予想される適正な応答速度よりも速くしておくことを特徴とする。
【0020】
本発明に従えば、整圧器の制御の応答速度を予想される適正な応答速度よりも速くしておくので、調整の初期には指標が予め定める範囲から逸脱する程度が大きくなり、速い応答速度を徐々に減少させて適正な応答速度が得られるようにすることができる。応答速度が遅い状態から調整を開始すると、ハンチングが生じて指標が逸脱しても、応答速度が速い状態であると誤判定して、さらに応答速度が遅すぎる状態に調整してしまうおそれがある。
【0021】
【発明の実施の形態】
図1は、本発明の実施の一形態である2系列ガバナシステムの構成を示す。本実施形態では、図4と同様に、2系列ガバナシステムの第1系列のガバナ1の開度を規定値に保持するように、第2系列のガバナ2の動作状態を制御する。ガバナ1,2は、弁3,4がそれぞれ開閉して、一次管路10から二次管路20に供給されるガスの圧力を減圧し、一定の二次圧に保つように制御する。弁3,4では、弁体3a,4aと弁座3b,4bとの間の間隙が開度に対応する。弁体3a,4aは、弁棒3c,4cの下端にそれぞれ装着され、弁座3b,4bはガバナ1,2のケーシングにそれぞれ固定されている。弁棒3c,4cは、中間部でダイヤフラム3d,4dおよびばね3e,4eにそれぞれ接続されている。ダイヤフラム3d,4dおよびばね3e,4eは、ダイヤフラム室3f,4fにそれぞれ収納される。ダイヤフラム3d,4dは、ダイヤフラム室3f,4f内を、2つの部分に仕切っている。ダイヤフラム室3f,4fでダイヤフラム3d,4dによって仕切られる下側の空間には、一次管路10と二次管路20との間に接続されるパイロット弁5,6と絞り7,8との中間の圧力が導入される。ダイヤフラム室3f,4fでダイヤフラム3d,4dによって仕切られる上側の空間には、二次管路20からの二次圧が導入され、ばね3e,4eがそれぞれ収納される。このようなガバナ1,2は、パイロット弁5,6の設定圧力で、二次圧を制御することができる。
【0022】
本実施形態の2系列ガバナシステムでは、第1系列のガバナ1の弁開度は検出手段40によって検出し、図4と同様に、弁開度が80%を超えないように、第2系列のガバナ2が動作する。第2系列のガバナ2の制御は、パイロット弁6の設定圧力を、モータ50から伝達機構51を介する機械的な駆動によって行う。検出手段40が検出するガバナ1の弁開度に基づいてモータ50を電気的に駆動するために、コントローラ60が用いられる。コントローラ60には、サーボアンプ61が含まれる。サーボアンプ61は、検出手段40の開度検出出力に基づいて、モータ50を回転駆動する。
【0023】
本実施形態のサーボアンプ61は、利得を制御して応答速度を細かく多段階に調整することができる。応答速度の調整は、ガバナ2の動作状態に対応する指標として二次圧P2を圧力計62で検出し、その変動が予め設定される範囲から逸脱する程度を、コントローラ60内の逸脱判定手段63によって判定する。逸脱判定手段63によって逸脱の程度が大きいと判定されるときは、コントローラ60内の速度変更手段64がサーボアンプ61の応答速度を変更する。
【0024】
図2は、本実施形態によるサーボアンプ61の応答速度の変更についての基本的な考え方を示す。ステップs0から変更の制御手順を開始し、サーボアンプ61の応答速度は、適切であると予想される速度よりも速くしておく。ステップs1では所定期間内に二次圧P2が閾値をn回以上往復しているか否かを判断する。nは期間の長さに応じて設定する。たとえば、1分間に数回程度は許容する前提で設定する。ステップs1で所定期間内での二次圧P2の変動が少なく、閾値を往復する回数がnよりも小さいときは、ステップs1に戻って、二次圧P2の監視を続ける。ステップs1で、所定期間内での二次圧P2の変動が多く、閾値を往復する回数がn以上になるときは、ステップs2でサーボアンプ61の応答速度を小さくして、モータ50の制御スピードを1ランク下降させる。
【0025】
サーボアンプ61の応答速度を、ガバナ2に対して予想される適正な応答速度よりも速くしておくので、調整の初期には二次圧P2が予め定める範囲から逸脱する程度が大きく、応答速度を徐々に減少させて適正な応答速度が得られるようにすることができる。応答速度が遅い状態から調整を開始すると、ハンチングが生じて二次圧P2が逸脱しても、応答速度が速い状態であると誤判定して、さらに応答速度を下降させ、応答速度が遅すぎる状態にしてしまうおそれがある。
【0026】
図3は、二次圧P2を指標としてガバナ2の制御状態を調整する際の圧力範囲の設定の例を示す。二次圧P2としての目標圧力をpsとすると、二次圧P2の許容範囲として、上限pmaxと下限pminとが考えられる。目標圧力psと上限pmaxとの間に上側閾値puを設定し、サーボアンプ61の応答速度を少し遅くしておけば、二次圧P2の変動が大きく、少なくとも上側閾値puを超える頻度が大きくなる。サーボアンプ61の応答速度を下降させれば、二次圧puの変動が小さくなり、適正な範囲に収るようになる。
【0027】
二次圧P2の変動は、負荷に供給する流量の変動に応じても生じるので、都市ガスなどでは、1日の時間帯による流量変化、季節による流量変化などの影響を考慮し、上側閾値puをある程度の回数超えることは許容する。上側閾値puを季節によって変更したり、回数の判定基準を季節によって変更することもできる。また、二次圧P2の上側ばかりではなく、下側閾値plを設定して、上側閾値puと下側閾値plとの間の範囲から二次圧P2が逸脱するか否かを判定するようにすることもできる。
【0028】
なお、ガバナ2の動作状態を反映する指標として二次圧P2を用いているけれども、パイロット圧なども同様に指標として用いることができる。また、弁4の開度も指標として用いることもできる。さらに、本発明の考え方は、単独で動作するガバナや、3系列以上で動作する多系列ガバナシステムのガバナにも同様に適用し、適切な応答速度に設定することができる。また、ガバナの形式は、図1に示すようなもの以外でも同様に適用することができる。
【0029】
【発明の効果】
以上のように本発明によれば、整圧器の制御動作が反映される指標を検出し、指標が予め設定される範囲から逸脱する程度を、流体の供給流量の瞬間的な変動の影響を受けないように判定することができる。整圧器の制御の応答速度を、指標の逸脱の程度が予め定める基準の程度に接近する方向に、部分的に変化させるので、応答速度を少しずつ適正な状態に改善していくことができる。
【0030】
また本発明によれば、2つの整圧器間で一方の開度が大きく他方の開度が小さい状態と、一方の開度が小さく他方の開度が大きい状態とを繰返すような事態になるのを防ぎ、適正な制御状態となるようにすることができる。
【0031】
また本発明によれば、整圧器の制御動作が反映される指標として、検出が容易な開度や圧力を用いることができる。
【0032】
また本発明によれば、整圧器の制御の応答速度を予想される適正な応答速度よりも速くしておき、調整の初期には指標が予め定める範囲から逸脱する程度が大きくても、応答速度を徐々に減少させて適正な応答速度が得られるようにすることができる。
【図面の簡単な説明】
【図1】本発明の実施の一形態である2系列ガバナシステの構成を簡略化して示すブロック図である。
【図2】図1の2系列ガバナシステムでモータの制御スピードを調整する基本的な考え方を示すフローチャートである。
【図3】図1の逸脱判定手段が二次圧P2の変動が逸脱しているか否かを判定する考え方を示すグラフである。
【図4】先行出願の2系列ガバナシステムの構成を簡略化して示す配管系統図、およびその動作特性を示すグラフである。
【符号の説明】
1,2 ガバナ
3,4 弁
5,6 パイロット弁
10 一次管路
20 二次管路
40 検出手段
50 モータ
60 コントローラ
61 サーボアンプ
62 圧力計
63 逸脱判定手段
64 速度変更手段
[0001]
TECHNICAL FIELD OF THE INVENTION
The present invention adjusts the control state of a pressure regulator provided in a pipeline system for transporting a fluid to reduce a primary pressure to a secondary pressure and suppress a pressure fluctuation due to a flow rate fluctuation so as to obtain an appropriate responsiveness. The present invention relates to a pressure regulator control system.
[0002]
[Prior art]
Conventionally, in a pipeline system that transports fluid such as a city gas supply system, in order to supply fluid at a constant pressure to a load, the supplied primary pressure is reduced, and even if the flow rate changes, the secondary pressure is reduced. A pressure regulator for controlling the pressure fluctuation is provided. A pressure regulator is also called a governor.
[0003]
For example, in the case of city gas supplied to a residential area, the load increases during a time when cooking, bathing, and the like are frequently performed, but the load does not increase so much during other times. If the load is usually smaller than the peak load, a plurality of governors are often connected in parallel. In a multi-system governor system in which a plurality of governors are connected in parallel, an emergency shutoff valve is connected in series for each governor (for example, see Patent Document 1).
[0004]
4A shows a simplified configuration of a two-sequence governor system representing a multi-sequence governor system, and FIG. 4B shows its operation characteristics. Fluid such as city gas supplied from the primary conduit 10 is regulated in pressure by the two governors 11 and 12 and supplied to the load of the secondary conduit 20. Emergency shutoff valves 21 and 22 are connected to the governors 11 and 12, respectively. Fluid is supplied to the governors 11 and 12 from the primary line 10 at the primary pressure P1 via the emergency shutoff valves 21 and 22. The two-system governor system 30 includes a first system 31 including the governor 11 and the emergency shutoff valve 21, and a second system 32 including the governor 12 and the emergency shutoff valve 22. Each governor 11, 12 reduces the primary pressure P1 to near the secondary pressure P2. That is, P1> P2.
[0005]
If a failure or the like occurs in any of the governors 11 and 12 and the pressure reducing function is impaired, there is a possibility that a high primary pressure P1 may be applied to the secondary pipeline 20, so the emergency shutoff valves 21 and 22 are provided, respectively. Although not shown, the shutoff operation is performed by detecting an abnormal operation such as the secondary pressure of the governor 11 or 12. By shutting off the emergency shutoff valve on the system side including the governor in which the malfunction has occurred, the pressure increase in the secondary pipeline 20 is prevented. Usually, the emergency cutoff valves 21 and 22 are in a fully open state.
[0006]
The detection unit 40 detects, for example, a valve opening degree as an operation state of the governor 11 of the first series 31. The governor 12 of the second series 32 operates so that the valve opening of the governor 11 of the first series detected by the detection means 40 stays near the value set as the upper limit of the normal operation state.
[0007]
FIG. 4B shows the relationship between the flow rates of the governors 11 and 12 and the pressure on the secondary side. The flow rate of the fluid substantially corresponds to the valve opening. Each governor 11, 12 has an operation characteristic as shown as L11, L12, respectively. When the load is small, the operating characteristic L12 of the governor 12 of the second series 32 is set such that the governor 11 of the first series 31 operates and the governor 12 of the second series 32 waits. 11 is set to operate on a lower pressure side than the operation characteristic L11. However, the governor 11 of the second series 32 starts operating so that the governor 11 of the first series 31 sets the valve opening degree, for example, 80% as the upper limit of the normal operation state, and the governor 11 stays near the upper limit. . The set pressure of the governor 12 is adjusted so as to increase, and as a result, an operation characteristic as indicated by L20 is obtained.
[0008]
When the valve opening of the governor 11 of the first system 31 is larger than 80% of the upper limit, the set pressure of the governor 12 of the second system 32 is adjusted to increase, and the valve opening of the governor 12 increases, Fluid is also supplied to the load via governor 12. As a result, the valve opening degree of the governor 11 of the first series 31 is reduced, and it is possible to prevent the governor 11 from greatly exceeding the upper limit. When the valve opening of the governor 11 of the first series 31 becomes smaller than the upper limit due to the decrease of the load or the operation of the governor 12 of the second series 32, the set pressure of the governor 12 of the second series 32 decreases, and the valve opening becomes descend. If the load is within the upper limit of 80% of the valve opening of the governor 11 of the first system 31, the governor 12 of the second system 32 will be in the fully closed state with the valve opening being 0. That is, when the flow rate is small, only the governor 11 of the first system operates to perform the pressure regulation.
[0009]
[Patent Document 1]
JP-A-11-282543
[Problems to be solved by the invention]
In the two-system governor system 30 as shown in FIG. 4A, one governor 11 is used from a small flow area to a large flow area, and the other governor 12 is used in a large flow area. The governor 12 of the second series 32 is feedback-controlled so as to maintain the upper limit of the valve opening of the governor 11 of the first series 31 of 80%. Such feedback control involves an excessive response when the load changes.
[0011]
That is, the governor 12 of the second series 32 is controlled while adjusting its own set pressure so that the opening degree of the governor 11 of the first series 31 is maintained at a specified value. Done in If an output capable of responding to a feedback signal (input) such as an opening degree at a high speed is generated by the detection means 40 functioning as a controller, it is expected that agile and highly accurate control can be performed. . However, if the reaction is too fast, hunting due to over-response occurs. When hunting occurs, the control is not stabilized, and the fluctuation of the secondary pressure continues. Further, a governor valve or the like may be worn due to sliding of a mechanical part or may be fatigued due to repeated deformation, thereby shortening the service life. For these reasons, it is difficult to always maintain proper responsiveness in an environment where the load and the like change every moment.
[0012]
An object of the present invention is to provide a pressure regulator control system that can be adjusted to maintain appropriate responsiveness in an environment where a load or the like changes every moment.
[0013]
[Means for Solving the Problems]
The present invention provides a pressure regulator that controls the fluid supplied from the primary side to the secondary side under reduced pressure and controls the fluid pressure to maintain a predetermined secondary pressure with respect to the fluctuating supply flow rate. A pressure regulator control system that adjusts to
Indicator detecting means for detecting an indicator reflecting the control operation of the pressure regulator,
Departure determining means for determining the extent to which the index detected by the index detecting means deviates from a preset range within a period set in advance to a fluctuation cycle of the supply flow rate of the fluid,
Speed change means for partially changing the response speed of control of the pressure regulator according to the degree of deviation determined by the deviation determination means in a direction in which the degree of deviation approaches a predetermined reference degree. A pressure regulator control system characterized by the following.
[0014]
According to the present invention, a pressure regulator control system supplies a fluid supplied from the primary side to the secondary side while reducing the pressure, and controls the pressure regulator to maintain a predetermined secondary pressure with respect to the varying supply flow rate. In order to obtain a proper response, an index detecting unit, a deviation determining unit, and a speed changing unit are included. Since the index detecting means detects an index on which the control operation of the pressure regulator is reflected, the state of the control operation of the pressure regulator can be grasped based on the detected index. The deviation determining means determines the degree of deviation of the index detected by the index detecting means from the preset range within a period set in advance in a fluctuation cycle of the supply flow rate of the fluid. The degree of deviation of the index from the set range can be determined so as not to be affected by the dynamic fluctuation. The speed changing unit partially changes the response speed of the control of the pressure regulator according to the degree of deviation determined by the deviation determining unit in a direction in which the degree of deviation approaches a predetermined reference level. The response speed can be gradually improved to an appropriate state.
[0015]
Also, in the present invention, a plurality of the pressure regulators operate simultaneously and in parallel,
At least one pressure regulator performs a control operation of the secondary pressure such that an operation state of another pressure regulator is within a predetermined range.
[0016]
According to the present invention, if the response speed of the pressure regulator is made too fast, hunting occurs, and the result affects other pressure regulators, and the operating state of the pressure regulator also fluctuates. This fluctuation further causes a change in the response speed. Even when the load is stabilized, one of the two regulators has a large opening and the other has a small opening. There is a risk that the situation will be repeated with a large state. In such a situation, the index easily deviates from the set range, so that the response speed can be adjusted so as to reduce the deviation of the index, and an appropriate control state can be obtained.
[0017]
Further, in the present invention, the index detecting means detects at least one of the opening degree and the pressure of the pressure regulator as the index.
[0018]
According to the present invention, at least the opening or the pressure is detected as an index reflecting the control operation of the pressure regulator. In a control in which the pressure regulator keeps the secondary pressure constant even when the supply flow rate of the fluid fluctuates, the opening degree of the valve changes, and the opening degree of the valve changes depending on the pressure such as the secondary pressure and the pilot pressure. Since the opening is a mechanical displacement, it can be easily grasped. The pressure can be easily detected from a pipe or the like.
[0019]
In the present invention, the response speed of control of the pressure regulator is set to be faster than an expected appropriate response speed.
[0020]
According to the present invention, since the response speed of the pressure regulator control is set faster than the expected appropriate response speed, the degree of the index deviating from the predetermined range becomes large at the beginning of adjustment, and the fast response speed is increased. Can be gradually reduced so that an appropriate response speed can be obtained. If the adjustment is started from a state where the response speed is low, even if hunting occurs and the index deviates, there is a possibility that the response speed is erroneously determined to be a state where the response speed is high and the state is further adjusted to a state where the response speed is too slow. .
[0021]
BEST MODE FOR CARRYING OUT THE INVENTION
FIG. 1 shows a configuration of a two-system governor system according to an embodiment of the present invention. In the present embodiment, similarly to FIG. 4, the operation state of the second system governor 2 is controlled so that the opening degree of the first system governor 1 of the two system governor system is maintained at a specified value. The governors 1 and 2 control the valves 3 and 4 to open and close, respectively, to reduce the pressure of the gas supplied from the primary line 10 to the secondary line 20 to maintain a constant secondary pressure. In the valves 3 and 4, the gap between the valve bodies 3a and 4a and the valve seats 3b and 4b corresponds to the opening. The valve bodies 3a and 4a are mounted on lower ends of the valve rods 3c and 4c, respectively, and the valve seats 3b and 4b are fixed to casings of the governors 1 and 2, respectively. The valve stems 3c, 4c are connected to the diaphragms 3d, 4d and the springs 3e, 4e, respectively, at an intermediate portion. The diaphragms 3d and 4d and the springs 3e and 4e are housed in the diaphragm chambers 3f and 4f, respectively. The diaphragms 3d, 4d partition the inside of the diaphragm chambers 3f, 4f into two parts. In the lower space partitioned by the diaphragms 3d, 4d in the diaphragm chambers 3f, 4f, an intermediate space between the pilot valves 5, 6 connected between the primary pipeline 10 and the secondary pipeline 20 and the throttles 7, 8 is provided. Pressure is introduced. In the upper space partitioned by the diaphragms 3d, 4d in the diaphragm chambers 3f, 4f, a secondary pressure from the secondary pipeline 20 is introduced, and the springs 3e, 4e are stored, respectively. Such governors 1 and 2 can control the secondary pressure by the set pressure of the pilot valves 5 and 6.
[0022]
In the two-system governor system according to the present embodiment, the valve opening of the first system governor 1 is detected by the detection means 40, and the second system governor 1 is controlled so that the valve opening does not exceed 80% as in FIG. The governor 2 operates. The control of the governor 2 of the second system is performed by mechanically driving the set pressure of the pilot valve 6 from the motor 50 via the transmission mechanism 51. The controller 60 is used to electrically drive the motor 50 based on the valve opening of the governor 1 detected by the detection means 40. The controller 60 includes a servo amplifier 61. The servo amplifier 61 drives the motor 50 to rotate based on the opening detection output of the detection means 40.
[0023]
The servo amplifier 61 of the present embodiment can control the gain and finely adjust the response speed in multiple steps. The response speed is adjusted by detecting the secondary pressure P2 as an index corresponding to the operating state of the governor 2 with the pressure gauge 62, and determining the degree of the deviation from a preset range by a deviation determining means 63 in the controller 60. Determined by When the deviation determining unit 63 determines that the degree of deviation is large, the speed changing unit 64 in the controller 60 changes the response speed of the servo amplifier 61.
[0024]
FIG. 2 shows the basic concept of changing the response speed of the servo amplifier 61 according to the present embodiment. The control procedure of the change is started from step s0, and the response speed of the servo amplifier 61 is set to be higher than the speed expected to be appropriate. In step s1, it is determined whether the secondary pressure P2 has reciprocated the threshold value n times or more within a predetermined period. n is set according to the length of the period. For example, the setting is made on the assumption that several times per minute are allowed. In step s1, when the fluctuation of the secondary pressure P2 within the predetermined period is small and the number of times of reciprocating the threshold is smaller than n, the process returns to step s1 to continue monitoring the secondary pressure P2. In step s1, when the fluctuation of the secondary pressure P2 within the predetermined period is large and the number of times of reciprocating the threshold value becomes n or more, the response speed of the servo amplifier 61 is reduced in step s2, and the control speed of the motor 50 is reduced. Is lowered by one rank.
[0025]
Since the response speed of the servo amplifier 61 is set to be faster than the appropriate response speed expected for the governor 2, the secondary pressure P2 greatly deviates from a predetermined range at the beginning of the adjustment. Can be gradually reduced so that an appropriate response speed can be obtained. If adjustment is started from a state where the response speed is slow, even if hunting occurs and the secondary pressure P2 deviates, it is erroneously determined that the response speed is fast, and the response speed is further decreased, and the response speed is too slow. There is a possibility that it will be in a state.
[0026]
FIG. 3 shows an example of setting a pressure range when adjusting the control state of the governor 2 using the secondary pressure P2 as an index. Assuming that the target pressure as the secondary pressure P2 is ps, an upper limit pmax and a lower limit pmin are considered as allowable ranges of the secondary pressure P2. If the upper threshold value pu is set between the target pressure ps and the upper limit pmax, and the response speed of the servo amplifier 61 is slightly reduced, the fluctuation of the secondary pressure P2 is large, and the frequency of exceeding the at least the upper threshold value pu is increased. . If the response speed of the servo amplifier 61 is decreased, the fluctuation of the secondary pressure pu becomes small, and the secondary pressure pu falls within an appropriate range.
[0027]
Since the fluctuation of the secondary pressure P2 also occurs according to the fluctuation of the flow rate supplied to the load, in the case of city gas, etc., the upper threshold value pu is considered in consideration of the influence of the flow rate change due to the time of day, the seasonal flow rate change and the like. Is allowed to exceed a certain number of times. The upper threshold value pu can be changed depending on the season, and the criterion for the number of times can be changed depending on the season. In addition, not only the upper side of the secondary pressure P2, but also a lower threshold value pl is set to determine whether the secondary pressure P2 deviates from a range between the upper threshold value pu and the lower threshold value pl. You can also.
[0028]
Although the secondary pressure P2 is used as an index reflecting the operation state of the governor 2, a pilot pressure or the like can be used as an index similarly. Further, the opening degree of the valve 4 can also be used as an index. Further, the concept of the present invention can be similarly applied to a governor that operates independently or a governor of a multi-system governor system that operates with three or more systems, and can set an appropriate response speed. Further, the governor format can be similarly applied to those other than those shown in FIG.
[0029]
【The invention's effect】
As described above, according to the present invention, the index reflecting the control operation of the pressure regulator is detected, and the degree of the index deviating from the preset range is affected by the instantaneous fluctuation of the supply flow rate of the fluid. It can be determined that there is not. Since the response speed of control of the pressure regulator is partially changed in a direction in which the degree of deviation of the index approaches a predetermined reference level, the response speed can be gradually improved to an appropriate state.
[0030]
Further, according to the present invention, between the two pressure regulators, a state in which one opening is large and the other is small, and a state in which one opening is small and the other is large are repeated. Can be prevented and an appropriate control state can be obtained.
[0031]
Further, according to the present invention, it is possible to use an easily detected opening degree and pressure as an index reflecting the control operation of the pressure regulator.
[0032]
According to the present invention, the response speed of the pressure regulator control is set to be faster than an expected appropriate response speed, and even if the index deviates from a predetermined range in the initial stage of the adjustment, the response speed is increased. Can be gradually reduced so that an appropriate response speed can be obtained.
[Brief description of the drawings]
FIG. 1 is a simplified block diagram showing a configuration of a two-system governor system according to an embodiment of the present invention.
FIG. 2 is a flowchart showing a basic concept of adjusting a control speed of a motor in the two-system governor system of FIG. 1;
FIG. 3 is a graph showing a concept of determining whether or not the deviation of the secondary pressure P2 has deviated from the deviation determining means of FIG. 1;
FIG. 4 is a piping diagram showing a simplified configuration of a two-system governor system of the prior application, and a graph showing its operation characteristics.
[Explanation of symbols]
1, 2 governor 3, 4 valve 5, 6 pilot valve 10 primary line 20 secondary line 40 detecting means 50 motor 60 controller 61 servo amplifier 62 pressure gauge 63 departure judging means 64 speed changing means

Claims (4)

一次側から供給される流体を二次側に減圧して供給し、変動する供給流量に対して予め定める二次圧を保つように制御する整圧器を、適正な応答性が得られるように調整する整圧器制御システムであって、
整圧器の制御動作が反映される指標を検出する指標検出手段と、
指標検出手段によって検出される指標が予め設定される範囲から逸脱する程度を、予め流体の供給流量の変動周期以上に設定される期間内で判定する逸脱判定手段と、
逸脱判定手段の判定する逸脱の程度に応じて、整圧器の制御の応答速度を、該逸脱の程度が予め定める基準の程度に接近する方向に、部分的に変化させる速度変更手段とを含むことを特徴とする整圧器制御システム。
Adjust the pressure regulator to supply the fluid supplied from the primary side to the secondary side while reducing the pressure and to maintain the predetermined secondary pressure against the fluctuating supply flow rate so that appropriate responsiveness is obtained. Pressure regulator control system,
Indicator detecting means for detecting an indicator reflecting the control operation of the pressure regulator,
Deviation determination means for determining the degree that the index detected by the index detection means deviates from a preset range within a period set in advance to a fluctuation cycle of the supply flow rate of the fluid,
Speed changing means for partially changing the response speed of control of the pressure regulator according to the degree of deviation determined by the deviation determining means in a direction in which the degree of deviation approaches a predetermined reference degree. A pressure regulator control system characterized by the following.
前記整圧器は、複数が同時並行稼働し、
少なくとも1つの整圧器は、他の整圧器の稼働状態が予め定める範囲内となるように二次圧の制御動作を行うことを特徴とする請求項1記載の整圧器制御システム。
A plurality of the pressure regulators operate simultaneously in parallel,
The pressure regulator control system according to claim 1, wherein at least one pressure regulator performs a control operation of a secondary pressure such that an operation state of another pressure regulator is within a predetermined range.
前記指標検出手段は、前記整圧器の少なくとも開度または圧力の一方を前記指標として検出することを特徴とする請求項1または2記載の整圧器制御システム。The pressure regulator control system according to claim 1, wherein the index detection unit detects at least one of an opening degree and a pressure of the pressure regulator as the index. 前記整圧器の制御の応答速度は、予想される適正な応答速度よりも速くしておくことを特徴とする請求項1〜3のいずれかに記載の整圧器制御システム。The pressure regulator control system according to any one of claims 1 to 3, wherein a response speed of the pressure regulator control is faster than an expected appropriate response speed.
JP2003031009A 2003-02-07 2003-02-07 Pressure regulator control system Pending JP2004240840A (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100959923B1 (en) * 2009-10-30 2010-05-27 우성시스템 주식회사 System for controlling the gas pressure
KR101212075B1 (en) * 2011-01-19 2012-12-13 주식회사 경동도시가스 Slam shut-off system for gas pressure regulating device

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100959923B1 (en) * 2009-10-30 2010-05-27 우성시스템 주식회사 System for controlling the gas pressure
KR101212075B1 (en) * 2011-01-19 2012-12-13 주식회사 경동도시가스 Slam shut-off system for gas pressure regulating device

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