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JP4480552B2 - Flow control device and flow control method - Google Patents
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JP4480552B2 - Flow control device and flow control method - Google Patents

Flow control device and flow control method Download PDF

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JP4480552B2
JP4480552B2 JP2004333652A JP2004333652A JP4480552B2 JP 4480552 B2 JP4480552 B2 JP 4480552B2 JP 2004333652 A JP2004333652 A JP 2004333652A JP 2004333652 A JP2004333652 A JP 2004333652A JP 4480552 B2 JP4480552 B2 JP 4480552B2
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valve
flow rate
opening
steam supply
opening degree
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JP2006146436A (en
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博之 木下
親昌 鳥家
孝治 城戸
山本  和彦
敏和 角田
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Chugoku Electric Power Co Inc
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Description

本発明は、ボイラ装置から管路を経由して蒸気を圧送して供給するため系統にかかり、より詳細には、蒸気供給の際にその管路を流れる流量を調整するための流量調整弁を備える流量制御装置またはその方法に関するものである。   The present invention relates to a system for pumping and supplying steam from a boiler device via a pipeline, and more specifically, a flow rate adjusting valve for adjusting the flow rate flowing through the pipeline when supplying steam. The present invention relates to a flow control device or a method therefor.

図4は、従来における蒸気供給で用いられる管路の系統図である。この系統100で供給される蒸気12は、管路(母管)11を経由してボイラ10側から客先側13へと導かれる。この管路(母管)11上には、分岐点11aにおいて中圧タービン16側へと分岐する分岐管路15を備えており、この分岐点11aより客先13側に寄った位置には流量調節弁14が配置されている。   FIG. 4 is a system diagram of a pipe line used in conventional steam supply. The steam 12 supplied by the system 100 is guided from the boiler 10 side to the customer side 13 via a pipe line (parent pipe) 11. A branch pipe 15 that branches to the intermediate pressure turbine 16 side at the branch point 11a is provided on the pipe (mother pipe) 11, and a flow rate is provided at a position closer to the customer 13 side than the branch point 11a. A control valve 14 is arranged.

図4のような従来の蒸気供給プラントの系統では、管路上に開閉可能な流量調節弁14を設置しておき、通常時では「常時全開状態」になるように設定されているものの、流量超過時またはプラント保護動作時などの特定時においては、この弁14を開状態から閉状態へと変換する動作をさせて、プラントを保護する必要がある。ところが、このような流量調節弁14は、通常時では常に全開状態にして使用しているために、この弁14がスティック(固着化、膠着化)してしまい、弁が開状態のまま閉じないという状況が起こることがある。この流量調節弁14を閉じなければならないときに、この弁14が開から閉へと移行動作しなくなるということは、蒸気供給のためのプラント自体を保護することが出来なくなる、ということを意味する。
なお、本発明に関連する分野の特許文献としては、例えば次のようなものがある。
特開2002−4894号公報
In the system of the conventional steam supply plant as shown in FIG. 4, the flow control valve 14 that can be opened and closed is installed on the pipeline, and is set so as to be “always fully open” under normal conditions. At a specific time such as the time or the plant protection operation, it is necessary to protect the plant by performing an operation of converting the valve 14 from the open state to the closed state. However, since such a flow rate control valve 14 is always used in a fully open state during normal operation, the valve 14 is sticked (fixed or stuck), and the valve remains open and does not close. The situation may occur. When the flow control valve 14 has to be closed, the fact that the valve 14 does not shift from opening to closing means that the plant for supplying steam cannot be protected. .
In addition, as a patent document of the field | area relevant to this invention, there exist the following, for example.
JP 2002-4894 A

上述のように、従来の蒸気供給のためのシステム系統では、管路(流路)に設けられた流量調節弁14がスティック(固着)してしまって閉じなくなる場合があり、このようなスティック防止のためには、定期的な頻度を定めて、管路上に設置された流量調節弁14に開閉動作をさせて、スティック(固着)が無いことを確認するための点検をしなければない、という問題点があった。   As described above, in the conventional system for supplying steam, the flow rate control valve 14 provided in the pipe (flow path) may stick (stick) and cannot be closed. In order to achieve this, it is necessary to set a periodic frequency, open and close the flow control valve 14 installed on the pipe line, and perform an inspection to confirm that there is no stick (sticking). There was a problem.

本発明は前述の問題点に鑑みてなされたものであり、この流量調節弁14がスティック(固着)して開閉動作ができなくなるということを防ぎ、定期的な弁の開閉点検の必要を無くし、また、蒸気供給にかかわる系統のシステム効率化・低コスト化などにも寄与することのできる流量制御装置およびその方法を提供することをその目的とする。   The present invention has been made in view of the above-mentioned problems, and prevents the flow rate control valve 14 from sticking (adhering) to be unable to open and close, eliminating the need for periodic valve opening and closing checks, It is another object of the present invention to provide a flow rate control apparatus and method that can contribute to system efficiency and cost reduction of a system related to steam supply.

(1)ボイラ装置から流量調整弁を設けた管路を経由して蒸気を圧送して供給するため蒸気供給装置において、
前記管路の蒸気流量に応じて弁開度を弁開度に余裕度を加えた弁追従開度になるように制御するための前記流量調整弁と、前記管路を流れる流量を測定する手段と、を備え、
前記流量調整弁における0.0613MPaの弁圧損に基づいて、蒸気供給流量が40〜260t/hのときに弁開度が15〜100%となってグラフ化したときに直線状のライン(A)を示す各値を求める手段と、
前記ライン(A)の弁開度(%)に所定の余裕度を持たせて増加させた直線状のライン(B)を示す弁開度を、前記蒸気供給流量(t/h)に対する弁追従開度(%)として定める手段と、
前記流量調整弁の弁開度を、前記弁追従開度(%)に基づいて動作するよう制御する手段と、を備えるとともに、
前記弁追従開度(%)は、前記弁開度(%)に15〜25%の余裕度を加えて構成されることで、前記蒸気供給量が常用される40〜200t/hの範囲において前記流量調整弁が前記ライン(B)に従って常に動作するように設定され、この範囲以上で全開状態100%のままに設定される。
(1) In a steam supply device for pumping and supplying steam from a boiler device via a pipe line provided with a flow control valve,
Means for measuring the flow rate through the flow control valve, the conduit for controlling such that the valve following the opening plus the margin the valve opening to the valve opening in accordance with the steam flow of the conduit And comprising
Based on the valve pressure loss of 0.0613 MPa in the flow rate adjusting valve, when the steam supply flow rate is 40 to 260 t / h, the valve opening degree is 15 to 100%, and the straight line (A) Means for obtaining each value indicating
The valve opening indicating the linear line (B) increased by giving a predetermined margin to the valve opening (%) of the line (A) is set to follow the valve with respect to the steam supply flow rate (t / h). Means to determine the opening (%);
Means for controlling the valve opening of the flow rate adjusting valve to operate based on the valve follow-up opening (%),
The valve follow-up opening degree (%) is configured by adding a margin of 15 to 25% to the valve opening degree (%), so that the steam supply amount is in a range of 40 to 200 t / h. The flow rate adjusting valve is set so as to always operate according to the line (B), and is set to 100% fully open above this range.

(2)ボイラ装置から流量調整弁を設けた管路を経由して蒸気を圧送して供給するため蒸気供給装置において、
前記管路の蒸気流量に応じて弁開度を弁開度に余裕度を加えた弁追従開度になるように制御するための前記流量調整弁と、前記管路を流れる流量を測定する手段と、を備え、
前記流量調整弁における0.0613MPaの弁圧損に基づいて、蒸気供給流量が40〜260t/hのときに弁開度が15〜100%となってグラフ化したときに直線状のライン(A)を示す各値を求めるステップと、
前記ライン(A)の弁開度(%)に所定の余裕度を持たせて増加させた直線状のライン(B)を示す弁開度を、蒸気供給流量(t/h)に対する弁追従開度(%)として定めるステップと、
前記流量調整弁の弁開度を、前記蒸気供給流量(t/h)に対する前記弁追従開度(%)に基づいて制御するステップと、を備えるとともに、
前記弁追従開度(%)は、前記弁開度(%)に15〜25%の余裕度を加えて構成されることで、前記蒸気供給量が常用される40〜200t/hの範囲において前記流量調整弁が前記ライン(B)に従って常に動作するように設定され、この範囲以上で全開状態100%のままに設定される。
(2) In a steam supply device for supplying steam by pressure from a boiler device via a pipe line provided with a flow control valve,
Means for measuring the flow rate through the flow control valve, the conduit for controlling such that the valve following the opening plus the margin the valve opening to the valve opening in accordance with the steam flow of the conduit And comprising
Based on the valve pressure loss of 0.0613 MPa in the flow rate adjusting valve, when the steam supply flow rate is 40 to 260 t / h, the valve opening degree is 15 to 100%, and the straight line (A) Obtaining each value indicating
The valve opening degree indicating the linear line (B) increased by giving a predetermined margin to the valve opening degree (%) of the line (A) is opened to follow the valve with respect to the steam supply flow rate (t / h). The steps defined as degrees (%),
Controlling the valve opening degree of the flow rate adjustment valve based on the valve follow-up opening degree (%) with respect to the steam supply flow rate (t / h), and
The valve follow-up opening degree (%) is configured by adding a margin of 15 to 25% to the valve opening degree (%), so that the steam supply amount is in a range of 40 to 200 t / h. The flow rate adjusting valve is set so as to always operate according to the line (B), and is set to 100% fully open above this range.

本発明による流量制御装置またはその方法によれば、蒸気供給系統で流路上に付設された流量調節弁において、実流量に対して余裕を持った値の弁追従開度を定め、この流量調節弁をこれに基づいて常時追従制御させるよう構成した。これにより、流路上の流量調節弁は中間開度で常に動作できるようになり、この流量調節弁14がスティック(固着化)して開閉動作ができなくなるということを防止し、定期的な弁の開閉点検の必要が無くなる。   According to the flow control device or the method thereof according to the present invention, in the flow control valve provided on the flow path in the steam supply system, the valve follow-up opening having a value having a margin with respect to the actual flow is determined, and the flow control valve Based on this, it is configured to always follow-up control. As a result, the flow rate control valve on the flow path can always operate at an intermediate opening, and the flow rate control valve 14 is prevented from sticking (fixed) and cannot be opened and closed. No need for open / close inspection.

以下に、本発明による流量制御装置および流量制御方法にかかる好適な実施形態について、添付の図1〜3を参照して説明する。
図1は、本発明による流量制御装置の一実施形態にかかる蒸気供給のための系統図である。この系統200で供給される蒸気22は、管路(母管)21を経由してボイラ20側から客先側23へと導かれ、管路(母管)21上には、従来の系統図(図4)と同様に、流量調整弁24を備える。そして、本発明によるこの系統200では、流量調整弁24の下流側にある管路21'の流量を測定するための流量計(FX)27と、この流量計(FX)27からの測定信号に基づいて流量調整弁24の開閉を制御するための弁制御部28とを備え、この弁制御部28は指令信号28'を出力して流量調整弁24の開閉動作を制御する。
DESCRIPTION OF EXEMPLARY EMBODIMENTS Hereinafter, preferred embodiments of a flow rate control device and a flow rate control method according to the present invention will be described with reference to FIGS.
FIG. 1 is a system diagram for supplying steam according to an embodiment of a flow control device of the present invention. The steam 22 supplied by this system 200 is guided from the boiler 20 side to the customer side 23 via a pipe (mother pipe) 21, and a conventional system diagram is provided on the pipe (mother pipe) 21. Similar to FIG. 4, a flow rate adjustment valve 24 is provided. In this system 200 according to the present invention, a flow meter (FX) 27 for measuring the flow rate in the pipe 21 ′ on the downstream side of the flow rate adjustment valve 24 and the measurement signal from the flow meter (FX) 27 are used. And a valve control unit 28 for controlling the opening / closing of the flow rate adjusting valve 24, and this valve control unit 28 outputs a command signal 28 ′ to control the opening / closing operation of the flow rate adjusting valve 24.

図2は、図1の系統200において、蒸気供給の管路に設置された流量調節(調整)弁24の特性の一例を示す図である。
図2の上の表データは、流量調整弁24において、所定の弁圧損(MPa)の値に基づいて、蒸気供給流量(t/h)と弁開度(%)と関係を実測により求めたものである。
図2の下のグラフ図中のA線は、図2の上の表データを基にした、蒸気供給流量(t/h)−弁開度(%)を示すラインである。また、B線は弁追従開度(%)を示す線であり、A線における弁開度(%)に所定の余裕度(ここでは20%)を持たせて増加させた弁開度を、蒸気供給流量(t/h)に対する弁追従開度(%)として定めて、この関係をグラフ化して示したものである。これらのA線とB線とは、共に弁開度100%未満では略直線状のラインが得られている。
FIG. 2 is a diagram illustrating an example of characteristics of the flow rate adjusting (adjusting) valve 24 installed in the steam supply pipeline in the system 200 of FIG.
The upper table data in FIG. 2 is obtained by actually measuring the relationship between the steam supply flow rate (t / h) and the valve opening degree (%) based on a predetermined valve pressure loss (MPa) value in the flow rate adjusting valve 24. Is.
The line A in the lower graph of FIG. 2 is a line indicating the steam supply flow rate (t / h) -valve opening degree (%) based on the upper table data of FIG. Line B is a line indicating a valve follow-up opening degree (%), and the valve opening degree increased by giving a predetermined margin (here, 20%) to the valve opening degree (%) in the A line, This relationship is defined as a valve follow-up opening degree (%) with respect to the steam supply flow rate (t / h) and is shown in a graph. The A line and the B line are both substantially linear when the valve opening is less than 100%.

図2の下のグラフ図において、A線はa1−a2−a3を結んでプロットしたもので示され、B線はb1−b2−を結んでプロットしたもので示されるが、図2の上の表データを参照して、これらのデータをまとめて示すと次のとおりである。
蒸気供給流量(スプレ量含まず) 弁開度 弁追従開度(+20%)
a1 35.2t/h 15% 35% (b1点)
a2 100.1t/h 44% 64% (b2点)
a3 229.3t/h 100% 100% (b3点)
In the lower graph of FIG. 2, the A line is shown by plotting a1-a2-a3, and the B line is shown by plotting b1-b2-. With reference to the table data, these data are summarized as follows.
Steam supply flow rate (not including spray amount) Valve opening Valve following opening (+ 20%)
a1 35.2t / h 15% 35% (b1 point)
a2 100.1 t / h 44% 64% (b2 points)
a3 229.3t / h 100% 100% (b3 points)

図2の下のグラフ図において、地点毎に説明すると次のとおりである。
a1は、蒸気供給流量40t/hのときの値であって、弁圧損0.0613MPaとなる弁開度は15%であり、これに余裕度(ここでは20%)を持たせて増加させた弁追従開度(%)では、蒸気供給流量40t/hのときに弁追従開度35%(b1点)となる。
a2は、蒸気供給流量114t/hのときの値であって、弁圧損0.0613MPaとなる弁開度は44%であり、これに余裕度(ここでは20%)を持たせて増加させた弁追従開度(%)は、蒸気供給流量114t/hのときに弁追従開度64%(b2点)となる。
a3は、蒸気供給流量260t/hのときの値であって、弁圧損0.0613MPaとなる弁開度は100%であり、これに余裕度(ここでは20%)を持たせて増加させた弁追従開度(%)では、弁開度は100%以上に増加させることはできないので、蒸気供給流量260t/hのときに弁追従開度100%のままとなり、b3点はa3点とその位置が重なこととなる。
In the lower graph of FIG. 2, each point will be described as follows.
a1 is a value when the steam supply flow rate is 40 t / h, and the valve opening degree at which the valve pressure loss becomes 0.0613 MPa is 15%, which is increased with a margin (20% here). In the valve follow-up opening degree (%), the valve follow-up opening degree is 35% (b1 point) when the steam supply flow rate is 40 t / h.
a2 is a value when the steam supply flow rate is 114 t / h, and the valve opening degree at which the valve pressure loss becomes 0.0613 MPa is 44%, which is increased with a margin (20% here). The valve follow-up opening degree (%) becomes the valve follow-up opening degree 64% (b2 point) when the steam supply flow rate is 114 t / h.
a3 is a value when the steam supply flow rate is 260 t / h, and the valve opening degree at which the valve pressure loss becomes 0.0613 MPa is 100%, which is increased with a margin (20% here). Since the valve opening cannot be increased to 100% or more at the valve follow-up opening (%), the valve follow-up opening remains at 100% when the steam supply flow rate is 260 t / h. The position will be heavy.

また図1の系統200に戻ると、本発明では、流量調整弁24における所定の弁圧損(MPa)の値に基づいて実測して、蒸気供給流量(t/h)と弁開度(%)との関係を求めておき、この弁開度(%)に所定の余裕度(ここでは20%)を持たせて増加させた弁開度を弁追従開度(%)として定める。そして、この系統200での流量調整弁24の弁開度を、蒸気供給流量(t/h)に対する弁追従開度(%)として設定し、これらに基づいて、弁制御部24では、流量計27で実際に測定された蒸気供給流量(t/h)に対応する流量調整弁24の弁開度が、弁追従開度(%)となるように制御する。なお、この弁追従開度(%)としては、弁開度(%)に15〜25%の余裕度を加えて構成されるのが好適であることが、実験の結果確認されている。   Returning to the system 200 of FIG. 1, in the present invention, the steam supply flow rate (t / h) and the valve opening (%) are measured based on a predetermined valve pressure loss (MPa) value in the flow rate adjusting valve 24. The valve opening degree which is increased by giving a predetermined margin (here, 20%) to this valve opening degree (%) is determined as the valve following opening degree (%). Then, the valve opening degree of the flow rate adjusting valve 24 in the system 200 is set as a valve follow-up opening degree (%) with respect to the steam supply flow rate (t / h), and based on these, the valve control unit 24 sets the flow meter. The valve opening degree of the flow rate adjusting valve 24 corresponding to the steam supply flow rate (t / h) actually measured at 27 is controlled to be the valve follow-up opening degree (%). As a result of experiments, it has been confirmed that the valve follow-up opening (%) is preferably configured by adding a margin of 15 to 25% to the valve opening (%).

このように、本発明では弁追従開度(%)を設定して流量調整弁24を動作させることにより、流量調整弁24の開閉を常に中間開度でフレキシブルに追従制御できるようになり、弁のスティック(固着)を防止することができる。また、図2に示すように、弁追従開度(%)の設定にあたっては、蒸気供給量が常用される範囲(40〜200t/h)において流量調整弁24が常に動作するように設定され、また、客先の蒸気使用量が最も多くなる非定常時(200t/h以上)においては、圧力損失が小さくなるよう流量調整弁24を全開として設定する。   As described above, in the present invention, by setting the valve follow-up opening degree (%) and operating the flow rate adjusting valve 24, the opening and closing of the flow rate adjusting valve 24 can always be flexibly controlled with an intermediate opening amount. Can prevent sticking. Further, as shown in FIG. 2, in setting the valve follow-up opening degree (%), the flow rate adjusting valve 24 is set to always operate in a range in which the steam supply amount is regularly used (40 to 200 t / h). Further, in the non-steady state (200 t / h or more) when the customer's steam usage is the largest (200 t / h or more), the flow rate adjustment valve 24 is set to be fully opened so that the pressure loss is reduced.

図3は、本発明が適用可能な系統の例を示す図であって、蒸気供給系統図である。この図3の系統300で供給される蒸気32は、管路31を経由してボイラ30側から客先側33へと導かれ、管路31上に流量調整弁34と、流量調整弁34の下流側の管路31'での実流量を測定する流量計(FX)35とを備え、この流量計(FX)35からの測定信号に基づいて、余裕度を持った値に設定された弁追従開度(%)に従って、流量調整弁34の弁の開閉動作が制御される。なお、この図3の系統300においては、管路31上の流量調節弁34の上流側には、逆止弁36と蒸気供給元弁37とが直列に配置され、この流量調節弁34の下流側には温度計38が直列に配置されている。   FIG. 3 is a diagram showing an example of a system to which the present invention can be applied, and is a steam supply system diagram. The steam 32 supplied in the system 300 of FIG. 3 is guided from the boiler 30 side to the customer side 33 via the pipeline 31, and the flow rate adjustment valve 34 and the flow rate adjustment valve 34 are connected to the pipeline 31. A flow meter (FX) 35 for measuring the actual flow rate in the downstream pipe line 31 ', and a valve set to a value having a margin based on a measurement signal from the flow meter (FX) 35 The opening / closing operation of the flow rate adjusting valve 34 is controlled according to the follow-up opening degree (%). In the system 300 of FIG. 3, a check valve 36 and a steam supply source valve 37 are arranged in series on the upstream side of the flow rate adjustment valve 34 on the pipe 31, and downstream of the flow rate adjustment valve 34. On the side, a thermometer 38 is arranged in series.

この図3の系統300の管路31上の流量調節弁34は、通常時においては本発明による弁追従開度(%)に従って流量調節弁34の開閉動作が制御されるが、ある特定時においてこの流量調節弁34の開閉動作を別の設定にして制御することも可能である。
つぎに、その特定時の弁の動作の制御について、いくつかの例を挙げておく。
(1)温度計38の測定において供給蒸気温度が「高」のときには、一定時限後、流量調節弁34を「閉」とし、蒸気供給元弁38を「閉」とする。
(2)流量計35において蒸気供給可能量の超過のときは、流量調節弁34は蒸気供給可能量以下に「制限」動作をする。
(3)蒸気遮断動作のときには、流量調節弁34を「全閉」とする。
The flow control valve 34 on the pipe line 31 of the system 300 in FIG. 3 is normally controlled to open and close the flow control valve 34 according to the valve follow-up opening degree (%) according to the present invention. It is also possible to control the opening / closing operation of the flow rate adjusting valve 34 with different settings.
Next, some examples will be given for controlling the operation of the valve at the specific time.
(1) When the supply steam temperature is “high” in the measurement by the thermometer 38, the flow rate control valve 34 is set to “closed” and the steam supply source valve 38 is set to “closed” after a certain period of time.
(2) When the steam supply capacity exceeds the steam supply capacity in the flow meter 35, the flow control valve 34 performs a “restriction” operation below the steam supply capacity.
(3) During the steam shut-off operation, the flow control valve 34 is set to “fully closed”.

本発明による流量制御装置および流量制御方法は、蒸気を供給する系統において、管路上に設けられた流量調整弁がスティックすることのない流量制御システムとして広く適用することができ、とりわけ電気・エネルギー産業上での利用可能性は極めて大きい。   INDUSTRIAL APPLICABILITY The flow rate control device and the flow rate control method according to the present invention can be widely applied as a flow rate control system in which a flow rate adjusting valve provided on a pipe does not stick in a system for supplying steam. The above availability is extremely large.

本発明による流量制御装置または方法の一実施形態を示す系統図である。1 is a system diagram showing an embodiment of a flow control device or method according to the present invention. 本発明による流量制御装置または方法の一実施形態を説明するためのデータ図である。It is a data figure for demonstrating one Embodiment of the flow control apparatus or method by this invention. 本発明による流量制御装置または方法の別の実施形態を示す系統図である。It is a systematic diagram which shows another embodiment of the flow control apparatus or method by this invention. 従来の蒸気供給の流量制御を説明するための系統図である。It is a systematic diagram for demonstrating the flow control of the conventional steam supply.

符号の説明Explanation of symbols

200 系統
20 ボイラ
21、21’ 管路(母管)
22、22’ 蒸気の流れ
23 客先
24 流量調整弁
25 再熱蒸気管
26 タービン
27 流量計(FX)
28 弁制御部
A 弁開度(%)を示す線
B 弁追従開度(%)を示す線
200 system 20 boiler 21, 21 'pipeline (mother pipe)
22, 22 'Steam flow 23 Customer 24 Flow control valve 25 Reheat steam pipe 26 Turbine 27 Flow meter (FX)
28 Valve control unit
A Line indicating valve opening (%)
B Line indicating valve follow-up opening (%)

Claims (2)

ボイラ装置から流量調整弁を設けた管路を経由して蒸気を圧送して供給するため蒸気供給装置において、
前記管路の蒸気流量に応じて弁開度を弁開度に余裕度を加えた弁追従開度になるように制御するための前記流量調整弁と、前記管路を流れる流量を測定する手段と、を備え、
前記流量調整弁における0.0613MPaの弁圧損に基づいて、蒸気供給流量が40〜260t/hのときに弁開度が15〜100%となってグラフ化したときに直線状のライン(A)を示す各値を求める手段と、
前記ライン(A)の弁開度(%)に所定の余裕度を持たせて増加させた直線状のライン(B)を示す弁開度を、前記蒸気供給流量(t/h)に対する弁追従開度(%)として定める手段と、
前記流量調整弁の弁開度を、前記弁追従開度(%)に基づいて動作するよう制御する手段と、を備えるとともに、
前記弁追従開度(%)は、前記弁開度(%)に15〜25%の余裕度を加えて構成されることで、前記蒸気供給量が常用される40〜200t/hの範囲において前記流量調整弁が前記ライン(B)に従って常に動作するように設定され、この範囲以上で全開状態100%のままに設定されることを特徴とする流量制御装置。
In a steam supply device for supplying steam by pressure via a pipe line provided with a flow control valve from a boiler device,
Means for measuring the flow rate through the flow control valve, the conduit for controlling such that the valve following the opening plus the margin the valve opening to the valve opening in accordance with the steam flow of the conduit And comprising
Based on the valve pressure loss of 0.0613 MPa in the flow rate adjusting valve, when the steam supply flow rate is 40 to 260 t / h, the valve opening degree is 15 to 100%, and the straight line (A) Means for obtaining each value indicating
The valve opening indicating the linear line (B) increased by giving a predetermined margin to the valve opening (%) of the line (A) is set to follow the valve with respect to the steam supply flow rate (t / h). Means to determine the opening (%);
Means for controlling the valve opening of the flow rate adjusting valve to operate based on the valve follow-up opening (%),
The valve follow-up opening degree (%) is configured by adding a margin of 15 to 25% to the valve opening degree (%), so that the steam supply amount is in a range of 40 to 200 t / h. The flow rate control device is set so that the flow rate adjusting valve always operates according to the line (B), and is set to be 100% fully open above this range.
ボイラ装置から流量調整弁を設けた管路を経由して蒸気を圧送して供給するため蒸気供給装置において、
前記管路の蒸気流量に応じて弁開度を弁開度に余裕度を加えた弁追従開度になるように制御するための前記流量調整弁と、前記管路を流れる流量を測定する手段と、を備え、
前記流量調整弁における0.0613MPaの弁圧損に基づいて、蒸気供給流量が40〜260t/hのときに弁開度が15〜100%となってグラフ化したときに直線状のライン(A)を示す各値を求めるステップと、
前ライン(A)の記弁開度(%)に所定の余裕度を持たせて増加させた直線状のライン(B)を示す弁開度を、前記蒸気供給流量(t/h)に対する弁追従開度(%)として定めるステップと、
前記流量調整弁の弁開度を、前記弁追従開度(%)に基づいて動作させるよう制御するステップと、を備えるとともに、
前記弁追従開度(%)は、前記弁開度(%)に15〜25%の余裕度を加えて構成されることで、前記蒸気供給量が常用される40〜200t/hの範囲において前記流量調整弁が前記ライン(B)に従って常に動作するように設定され、この範囲以上で全開状態100%のままに設定されることを特徴とする流量制御方法。
In a steam supply device for supplying steam by pressure via a pipe line provided with a flow control valve from a boiler device,
Means for measuring the flow rate through the flow control valve, the conduit for controlling such that the valve following the opening plus the margin the valve opening to the valve opening in accordance with the steam flow of the conduit And comprising
Based on the valve pressure loss of 0.0613 MPa in the flow rate adjusting valve, when the steam supply flow rate is 40 to 260 t / h, the valve opening degree is 15 to 100%, and the straight line (A) Obtaining each value indicating
A valve opening degree indicating a linear line (B) increased by giving a predetermined margin to the valve opening degree (%) of the previous line (A) is a valve for the steam supply flow rate (t / h). A step determined as a follow-up opening (%);
And controlling the valve opening of the flow rate adjusting valve to operate based on the valve follow-up opening (%),
The valve follow-up opening degree (%) is configured by adding a margin of 15 to 25% to the valve opening degree (%), so that the steam supply amount is in a range of 40 to 200 t / h. The flow rate control method is characterized in that the flow rate adjusting valve is set so as to always operate according to the line (B), and is set to 100% in a fully open state above this range.
JP2004333652A 2004-11-17 2004-11-17 Flow control device and flow control method Expired - Lifetime JP4480552B2 (en)

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