JP5842492B2 - Boiler system - Google Patents

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JP5842492B2
JP5842492B2 JP2011202068A JP2011202068A JP5842492B2 JP 5842492 B2 JP5842492 B2 JP 5842492B2 JP 2011202068 A JP2011202068 A JP 2011202068A JP 2011202068 A JP2011202068 A JP 2011202068A JP 5842492 B2 JP5842492 B2 JP 5842492B2
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茂昭 西岡
茂昭 西岡
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Miura Co Ltd
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Description

この発明は、複数の蒸気ボイラの燃焼を台数制御器により制御するボイラシステムに関するものである。   The present invention relates to a boiler system that controls combustion of a plurality of steam boilers by a number controller.

蒸気ボイラは、長時間の運転により缶水が濃縮する。特許文献1などに記載のように、この濃縮が過度に進行しないように、積算燃焼時間に応じて缶水のブローを行う。   Steam boilers concentrate in long-term operation. As described in Patent Document 1, etc., can water is blown according to the accumulated combustion time so that the concentration does not proceed excessively.

この出願の発明者は、こうした積算燃焼時間に応じたブローを、複数の蒸気ボイラの燃焼を台数制御器による制御するボイラシステムに適用すると、つぎの課題があることを見出した。   The inventor of this application has found that there is the following problem when the blow according to the accumulated combustion time is applied to a boiler system that controls the combustion of a plurality of steam boilers by a number controller.

すなわち、各蒸気ボイラは、蒸気ヘッダ内の圧力(第一圧力)に基づく台数制御器からの燃焼指示信号により燃焼を行うが、各蒸気ボイラの缶体内の圧力(第二圧力)が第一圧力よりも低いと、各蒸気ボイラから蒸気ヘッダへ蒸気の流出がない,すなわち缶水の濃縮が生じていないにも拘らず、燃焼しているので、ブロー制御の積算燃焼時間にカウントされてしまう。このため必要以上にブローが行われることになり、熱的なロスが多くなるとともに、缶水の濃縮不足を招くことになる。   That is, each steam boiler burns by a combustion instruction signal from the number controller based on the pressure in the steam header (first pressure), but the pressure (second pressure) in the can body of each steam boiler is the first pressure. If it is lower than that, since there is no outflow of steam from each steam boiler to the steam header, that is, although the can water is not concentrated, combustion is performed, so that it is counted as an integrated combustion time of blow control. For this reason, blow is performed more than necessary, resulting in an increase in thermal loss and insufficient concentration of the can water.

実公平7−49208号公報No. 7-49208

この発明が解決しようとする課題は、必要以上のブローを防止し、熱的なロスを減少するとともに、缶水の濃縮不足を防止することである。   The problem to be solved by the present invention is to prevent blowing more than necessary, reduce thermal loss, and prevent insufficient concentration of canned water.

この発明は、前記課題を解決するためになされたもので、請求項1に記載の発明は、複数台の蒸気ボイラと、前記各蒸気ボイラから前記各蒸気ボイラの蒸気が集合する蒸気集合部と、前記各蒸気ボイラに設けられ自らの積算燃焼時間に応じて缶水のブローを制御するボイラ制御器と、前記各ボイラ制御器へ燃焼指示信号を送信して燃焼を制御する台数制御器とを備え、前記台数制御器は、前記蒸気集合部の第一圧力に応じて前記各ボイラ制御器へ燃焼指示信号を送信して燃焼を制御するように構成され、前記各ボイラ制御器は、燃焼中であって、前記蒸気集合部への蒸気の流出が前記各蒸気ボイラの缶体内の第二圧力と前記第一圧力との比較で無いと判断したとき、ブロー制御のための積算燃焼時間としてカウントしないことを特徴としている。 This invention was made in order to solve the above-mentioned subject, and the invention according to claim 1 includes a plurality of steam boilers, and a steam collecting portion where steam of each steam boiler gathers from each steam boiler. A boiler controller that is provided in each steam boiler and controls the blow of canned water according to its accumulated combustion time; and a number controller that controls combustion by transmitting a combustion instruction signal to each of the boiler controllers. The number controller is configured to control combustion by transmitting a combustion instruction signal to each boiler controller according to a first pressure of the steam collecting portion, and each boiler controller is in combustion a is, when the outflow of steam into the steam collecting unit determines that the not a comparison between the second pressure and the first pressure of the can body of the steam boiler, counted as the integrated burn time for the blow control It is characterized by not .

請求項1に記載の発明よれば、前記各蒸気ボイラが燃焼中であっても前記各蒸気ボイラから蒸気が流出してない間は、前記積算燃焼時間にカウントしないので、必要以上のブローが防止される。また、前記各ボイラ制御器による蒸気の流出が無いとの判断が、前記第一圧力と前記第二圧力との検出により可能となるので、流量センサにより検出するものと比較して、システムの構成を簡素化することができるという効果を奏する。 According to the first aspect of the present invention, even when the steam boilers are in combustion, while the steam does not flow out from the steam boilers, the accumulated combustion time is not counted. Is done. In addition, since it is possible to determine that there is no outflow of steam by each of the boiler controllers by detecting the first pressure and the second pressure, the system configuration is compared with that detected by the flow sensor. There is an effect that can be simplified.

記各ボイラ制御器による蒸気の流出が無いとの判断は、前記各蒸気ボイラの缶体内の第二圧力が前記第一圧力より低い間に行われる。 Before Symbol determines the outflow of steam due to absence each boiler controller, the second pressure of the can body of the steam boiler is made between lower than the first pressure.

この発明によれば、必要以上のブローを防止し、熱的なロスを減少するとともに、缶水の濃縮不足を防止することができる。   According to this invention, blow more than necessary can be prevented, thermal loss can be reduced, and insufficient concentration of canned water can be prevented.

この発明を実施したボイラシステムの実施の形態の概略構成図である。It is a schematic block diagram of embodiment of the boiler system which implemented this invention. 同実施の形態の制御プログラムを説明するフローチャート図である。It is a flowchart figure explaining the control program of the embodiment.

(実施の形態の構成)
以下、この発明の実施の形態のボイラシステム1を図面に基づいて詳細に説明する。ボイラシステム1は、段階的な燃焼位置にて蒸発量を制御可能とされる複数台(この実施の形態では3台)の蒸気ボイラ(以下、単にボイラという。)2A,2B,2Cと、各ボイラ2A,2B,2Cを蒸気管(符号省略)で連結する共通の蒸気ヘッダ3と、蒸気ヘッダ3の内部の蒸気圧力を検出するための圧力検出器4と、第一圧力検出器4の検出圧力(第一圧力)P1に応じて、予め記憶した台数制御プログラムに基づき、予め設定しておいた起動順序に従って必要台数のボイラを燃焼・停止させ、蒸気負荷の変化に追随するように制御する台数制御器5とを備えている。蒸気ヘッダ3は、この発明のボイラ2A,2B,2Cからの蒸気が集合する蒸気集合部であり、蒸気使用機器6と蒸気管(符号省略)で連結されている。
(Configuration of the embodiment)
Hereinafter, a boiler system 1 according to an embodiment of the present invention will be described in detail with reference to the drawings. The boiler system 1 includes a plurality of (three in this embodiment) steam boilers (hereinafter simply referred to as boilers) 2A, 2B, and 2C that are capable of controlling the amount of evaporation at stepwise combustion positions. A common steam header 3 for connecting the boilers 2A, 2B, 2C with steam pipes (not shown), a pressure detector 4 for detecting the steam pressure inside the steam header 3, and detection by the first pressure detector 4 In accordance with the pressure (first pressure) P1, a required number of boilers are combusted and stopped in accordance with a preset startup sequence based on a previously stored number control program, and control is performed so as to follow a change in steam load. A number controller 5 is provided. The steam header 3 is a steam collecting part where steam from the boilers 2A, 2B, 2C of the present invention is collected, and is connected to the steam using device 6 by a steam pipe (reference numeral omitted).

各ボイラ2A,2B,2Cには、それぞれバーナ(図示省略)の燃焼によって、蒸気を生成する缶体7A,7B,7Cと、各缶体7A,7B,7C内の圧力を検出する第二圧力検出器8A,8B,8Cと、ブロー制御用の弁9A,9B,9Cを有する排水路(ブローライン)10A,10B,10Cと、予め記憶した制御プログラムにより、第二圧力検出器8A,8B,8Cの検出圧力(第二圧力)P2など信号に基づき、弁(ブロー弁)9A,9B,9Cなどを制御するボイラ制御器11A,11B,11Cとを備えている。   Each boiler 2A, 2B, 2C has a can 7A, 7B, 7C that generates steam by combustion of a burner (not shown), and a second pressure that detects the pressure in each can 7A, 7B, 7C. Second pressure detectors 8A, 8B, 8C, 8A, 8B, 8C, drainage channels (blow lines) 10A, 10B, 10C having valves 9A, 9B, 9C for blow control, and a control program stored in advance. Boiler controllers 11A, 11B, and 11C that control valves (blow valves) 9A, 9B, and 9C based on signals such as the detected pressure (second pressure) P2 of 8C are provided.

各ボイラ制御器11A,11B,11Cによる制御プログラムには、燃焼制御や水位制御に加えて、濃縮ブロー制御を含んでいる。濃縮ブロー制御は、周知の制御であり、台数制御器5からの燃焼指示信号に基づき、ボイラ2A,2B,2Cが燃焼した時間を計測し、燃焼時間Tを積算して、この積算燃焼時間Tに基づき缶体7A,7B,7C内の缶水の濃縮度を算出し、算出した濃縮度が所定の値を越えると濃縮ブロー量を算出して濃縮ブローを実行する制御である。なお、濃縮ブローを行う場合、各ボイラ制御器11A,11B,11Cは、算出した濃縮度に対応する時間分だけ各弁9A,9B,9Cを開くことで、濃縮した缶水を排水路10A,10B,10Cを通して排出する。   The control program by each boiler controller 11A, 11B, 11C includes concentration blow control in addition to combustion control and water level control. The enrichment blow control is a well-known control. Based on the combustion instruction signal from the number controller 5, the time when the boilers 2A, 2B, 2C are burned is measured, the combustion time T is integrated, and this integrated combustion time T Based on the above, the concentration of the can water in the can bodies 7A, 7B, 7C is calculated, and when the calculated concentration exceeds a predetermined value, the concentration blow amount is calculated and the concentration blow is executed. In addition, when performing concentration blow, each boiler controller 11A, 11B, 11C opens each valve 9A, 9B, 9C for the time corresponding to the calculated enrichment, and drains 10A, Discharge through 10B and 10C.

この発明は、濃縮ブロー制御における積算燃焼時間Tの算出制御に特徴があり、積算燃焼時間Tに基づき、濃縮ブロー量を算出するもの,すなわち積算燃焼時間Tが長いほど濃縮ブロー量が多くなるものであれば、濃縮ブロー量の算出および濃縮ブロー量による濃縮ブローの制御をどのように行うかは問わない。   The present invention is characterized in the control for calculating the integrated combustion time T in the concentrated blow control, and calculates the concentrated blow amount based on the integrated combustion time T, that is, the longer the integrated combustion time T, the larger the concentrated blow amount. If so, it does not matter how to calculate the concentration blow amount and control the concentration blow by the concentration blow amount.

そして、積算燃焼時間Tの算出制御の特徴とするところは、台数制御器5からの指示信
号による燃焼中であって、各ボイラ2A,2B,2Cから蒸気ヘッダ3への蒸気の流出が無いと判断したとき、ブロー制御のための積算燃焼時間Tとしてカウントせず、蒸気の流出が有りと判断したとき、ブロー制御のための積算燃焼時間Tとしてカウントするところにある。
The feature of the calculation control of the integrated combustion time T is that combustion is being performed by an instruction signal from the number controller 5, and there is no outflow of steam from each boiler 2A, 2B, 2C to the steam header 3. When it is determined, it is not counted as the cumulative combustion time T for blow control, and when it is determined that there is steam outflow, it is counted as the cumulative combustion time T for blow control.

そして、この実施の形態では、各ボイラ制御器11A,11B,11Cは、指示信号による燃焼中であって、各蒸気ボイラの缶体内の第二圧力P2と第一圧力P1との比較で行われる。具体的には、各ボイラ2A,2B,2Cの第二圧力P2が第一圧力P1より低い状態が設定時間(例えば5秒)継続すると「蒸気の流出が無い」と判断する。第二圧力P2が第一圧力P1より高いと「蒸気の流出が有る」と判断する。この積算燃焼時間Tの算出制御の一例を図2に示す。   And in this embodiment, each boiler controller 11A, 11B, 11C is performing combustion by an instruction | indication signal, Comprising: It is performed by the comparison with the 2nd pressure P2 in the can body of each steam boiler, and the 1st pressure P1. . Specifically, if the state where the second pressure P2 of each boiler 2A, 2B, 2C is lower than the first pressure P1 continues for a set time (for example, 5 seconds), it is determined that “there is no outflow of steam”. When the second pressure P2 is higher than the first pressure P1, it is determined that “there is steam outflow”. An example of calculation control of this integrated combustion time T is shown in FIG.

また、台数制御器5による台数制御プログラムは、周知の制御であり、負荷量に対応した燃焼台数制御であって、第一圧力信号により必要燃焼台数を決定し、各ボイラ制御器11A,11B,11Cに対して燃焼指示または燃焼停止(燃焼待機を含む)の信号を出す制御である。   The number control program by the number controller 5 is a well-known control, and is a combustion number control corresponding to the load amount. The required number of combustion is determined by the first pressure signal, and each boiler controller 11A, 11B, This is a control for outputting a combustion instruction or combustion stop (including combustion standby) signal to 11C.

台数制御は、たとえば、特公平6−92804号公報に示されるような制御とするが、これに限定されるものではない。また、各ボイラ2の燃焼制御方式は、停止状態、低燃焼状態(第一燃焼位置)L、高燃焼状態(第二燃焼位置)H、の三位置だけではなく、4位置制御方式や2位置制御方式とすることができる。また、3位置制御などの段階制御方式だけではなく、無段階制御方式とすることができる。   The number control is, for example, control as disclosed in Japanese Patent Publication No. 6-92804, but is not limited thereto. The combustion control system of each boiler 2 is not limited to the three positions of the stop state, the low combustion state (first combustion position) L, and the high combustion state (second combustion position) H. It can be a control method. In addition, a stepless control method such as a three-position control can be used.

(実施の形態の動作)
つぎに、この実施の形態の濃縮ブロー動作を図2に基づき説明する。今、台数制御器5からの燃焼指示信号により、予め設定しておいた起動順序(起動優先順位)に基づき、ボイラ2Aのみが燃焼していたとする。そして、蒸気負荷の増加を第一圧力検出器4にて検出して、燃焼待機中のボイラ2Bに対して新たに燃焼指示信号が出されたとする。
(Operation of the embodiment)
Next, the concentration blow operation of this embodiment will be described with reference to FIG. Now, it is assumed that only the boiler 2 </ b> A is combusting based on a preset starting order (starting priority order) based on a combustion instruction signal from the number controller 5. Then, it is assumed that an increase in the steam load is detected by the first pressure detector 4 and a combustion instruction signal is newly issued to the boiler 2B on standby for combustion.

図2を参照して、ボイラ2Bのボイラ制御器11Bは、ステップS1(以下、ステップSNを単にSNという。)にて、YESを判定し、ボイラ2Bは、燃焼を開始する。そして、S2へ移行して、第二圧力P2が第一圧力P1より小さいかどうかを判定する。P2>P1の場合、ボイラ2Bの缶体7Bから蒸気ヘッダ3へ向けて蒸気が流出しているので、S3へ移行して、濃縮ブロー制御のための積算燃焼時間Tとしてカウントする。   Referring to FIG. 2, boiler controller 11B of boiler 2B determines YES in step S1 (hereinafter, step SN is simply referred to as SN), and boiler 2B starts combustion. And it transfers to S2 and it is determined whether the 2nd pressure P2 is smaller than the 1st pressure P1. In the case of P2> P1, since the steam is flowing out from the can 7B of the boiler 2B toward the steam header 3, the process proceeds to S3 and is counted as an integrated combustion time T for the concentrated blow control.

P1>P2は、ボイラ2Bが燃焼をしばらく停止している状態での起動(冷態起動)時に生ずる。P1>P2が所定時間継続すると、S2でYESが判定され、S4へ移行する。S4では、ボイラ2Bが燃焼しているにもかかわらず、積算燃焼時間Tとしてカウントしない。なお、P1>P2は、台数制御器5からの指示信号による待機制御の一つである圧力保持制御時にも生ずる。待機制御は、各ボイラを負荷追従性が良い状態にしておく制御であり、圧力保持制御は、蒸気供給に寄与しない圧力で予め暖気状態として応答性を高めることを目的とした制御である。   P1> P2 occurs at the time of startup (cold startup) in a state where the boiler 2B has stopped combustion for a while. If P1> P2 continues for a predetermined time, YES is determined in S2, and the process proceeds to S4. In S4, the accumulated combustion time T is not counted even though the boiler 2B is burning. Note that P1> P2 also occurs during pressure holding control, which is one of standby control based on an instruction signal from the number controller 5. The standby control is control for keeping each boiler in a state where the load followability is good, and the pressure holding control is control for the purpose of enhancing the responsiveness as a warm-up state in advance with a pressure that does not contribute to steam supply.

このように、P1>P2の状態では、ボイラ2Bが燃焼しているにもかかわらず、缶体7B内の蒸気が蒸気ヘッダ3へ流れない,すなわち缶水の濃縮が生じていないので、濃縮ブロー量を決める積算燃焼時間Tとしてカウントしない。これによって、P1>P2であっても積算燃焼時間Tとしてカウントするものと比較して、必要以上に積算燃焼時間Tを増加させないことになる。その結果、必要以上に、濃縮ブローを行うことを防止できる。そして、必要以上の缶水の排出が防止されるので、熱的なロスを低減できるとともに、缶水の濃縮不足を防止できる。   In this way, in the state of P1> P2, the steam in the can 7B does not flow to the steam header 3 although the boiler 2B is combusting, that is, no concentration of the can water has occurred. The cumulative combustion time T that determines the amount is not counted. As a result, even if P1> P2, the cumulative combustion time T is not increased more than necessary as compared with the case where the cumulative combustion time T is counted. As a result, it is possible to prevent the concentration blow from being performed more than necessary. And since unnecessary discharge of can water is prevented, thermal loss can be reduced and insufficient concentration of can water can be prevented.

この発明は、前記実施の形態に限定されるものではなく、各ボイラ制御器11A,11B,11Cによる「蒸気の流出が無い」との判断は、前記実施の形態では、台数制御器5からの指示信号による燃焼中であって、各ボイラ2A,2B,2Cの第二圧力P2が第一圧力P1より低い間としているが、これに限定されないものであり、各ボイラ2A,2B,2Cの缶体7A,7B,7Cから蒸気ヘッダ3に至る管路(符号省略)に蒸気の流れを検出する流量センサ(図示省略)を設けて、この流量センサにより「蒸気の流出が無い」を判断するように構成することができる。   The present invention is not limited to the above-described embodiment, and the determination that “there is no outflow of steam” by each of the boiler controllers 11A, 11B, and 11C is from the number controller 5 in the above-described embodiment. While the combustion is performed by the instruction signal, the second pressure P2 of each boiler 2A, 2B, 2C is lower than the first pressure P1, but this is not a limitation, and each boiler 2A, 2B, 2C can A flow rate sensor (not shown) for detecting the flow of steam is provided in the pipe line (not shown) from the bodies 7A, 7B, 7C to the steam header 3, so that “no steam outflow” is judged by this flow rate sensor. Can be configured.

2A,2B,2C 蒸気ボイラ(ボイラ)
3 蒸気ヘッダ(蒸気集合部)
4 第一圧力検出器
5 台数制御器
8A,8B,8C 第二圧力検出器
2A, 2B, 2C Steam boiler (boiler)
3 Steam header (steam collecting part)
4 First pressure detector 5 Number controller 8A, 8B, 8C Second pressure detector

Claims (1)

複数台の蒸気ボイラと、
前記各蒸気ボイラから前記各蒸気ボイラの蒸気が集合する蒸気集合部と、
前記各蒸気ボイラに設けられ自らの積算燃焼時間に応じて缶水のブローを制御するボイラ制御器と、
前記各ボイラ制御器へ燃焼指示信号を送信して燃焼を制御する台数制御器とを備え、
前記台数制御器は、前記蒸気集合部の第一圧力に応じて前記各ボイラ制御器へ燃焼指示信号を送信して燃焼を制御するように構成され、
前記各ボイラ制御器は、燃焼中であって、前記蒸気集合部への蒸気の流出が前記各蒸気ボイラの缶体内の第二圧力と前記第一圧力との比較で無いと判断したとき、ブロー制御のための積算燃焼時間としてカウントしないことを特徴とするボイラシステム。
Multiple steam boilers,
A steam collecting portion where the steam of each steam boiler gathers from each steam boiler;
A boiler controller that is provided in each steam boiler and controls the blow of canned water according to its accumulated combustion time;
A unit controller for controlling combustion by transmitting a combustion instruction signal to each of the boiler controllers,
The number controller is configured to control combustion by transmitting a combustion instruction signal to the boiler controllers according to a first pressure of the steam collecting portion,
Each boiler controller, a combustion, when the outflow of steam into the steam collecting unit determines that the not a comparison between the second pressure and the first pressure of the can body of the steam boiler, blow A boiler system that is not counted as an integrated combustion time for control.
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