JPH0232525B2 - - Google Patents
Info
- Publication number
- JPH0232525B2 JPH0232525B2 JP57044610A JP4461082A JPH0232525B2 JP H0232525 B2 JPH0232525 B2 JP H0232525B2 JP 57044610 A JP57044610 A JP 57044610A JP 4461082 A JP4461082 A JP 4461082A JP H0232525 B2 JPH0232525 B2 JP H0232525B2
- Authority
- JP
- Japan
- Prior art keywords
- economizer
- temperature
- water supply
- feed water
- boiler
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
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- Control Of Steam Boilers And Waste-Gas Boilers (AREA)
Description
【発明の詳細な説明】
<産業上の利用分野>
この発明はボイラ装置、特に節炭器の低温腐食
を防止する手段を設けたボイラ装置に関する。DETAILED DESCRIPTION OF THE INVENTION <Industrial Application Field> The present invention relates to a boiler system, and particularly to a boiler system provided with a means for preventing low-temperature corrosion of an economizer.
<従来の技術及びその問題点>
ボイラを構成する部材については硫黄分を含有
する燃料を使用するときは排ガス中に亜硫酸ガス
(SO3)を含むこととなり、この排ガスが低温部
材に接触するときその含有する蒸気は露点に達し
凝縮しこれにSO3が溶け込み硫酸となりその部材
を腐食し、事故に発展するものである。このよう
な部材としては空気予熱器、節炭器、ダクトを形
成する鋼板等が該当するものであることは知られ
ている。このうち圧力をもつ給水を加熱する節炭
器の伝熱管に腐食により漏水を生ずるときは運転
停止をして休缶し節炭器の補修または交換させね
ばならぬという問題がある。<Prior art and its problems> When using fuel containing sulfur in the parts that make up a boiler, the exhaust gas contains sulfur dioxide gas (SO 3 ), and when this exhaust gas comes into contact with low-temperature parts. The steam it contains reaches its dew point and condenses, and SO 3 dissolves into it to form sulfuric acid, which corrodes the parts and leads to an accident. It is known that such members include air preheaters, energy savers, steel plates forming ducts, and the like. Among these problems, when water leaks due to corrosion in the heat exchanger tubes of the energy saver that heats the pressurized water supply, there is a problem in that the operation must be shut down, the tank shut down, and the energy saver repaired or replaced.
第1図は炭素鋼チユーブで内部に給水が流れて
いる場合において、重油燃料中の硫黄含有量
(%)を横軸とし縦軸に腐食防止最低チユーブメ
タル温度をとつたときの線図である。チユーブメ
タル温度は伝熱管内にスケールのない場合はほぼ
管内流体の温度と考えてよい。曲線イは重油燃焼
ボイラの場合で燃料中にバナジウムを含まぬ場合
の腐食防止最低チユーブメタル温度を示し、曲線
ロは燃焼残渣(灰分)中に含有するバナジウムが
約3.5%の場合の腐食防止最低チユーブメタル温
度を示す。 Figure 1 is a diagram of a carbon steel tube with feed water flowing inside, with the horizontal axis representing the sulfur content (%) in heavy oil fuel and the vertical axis representing the minimum tube metal temperature for preventing corrosion. . If there is no scale inside the heat transfer tube, the tube metal temperature can be considered to be approximately the temperature of the fluid inside the tube. Curve A shows the minimum tube metal temperature for preventing corrosion when the fuel does not contain vanadium in the case of a heavy oil-fired boiler, and curve B shows the minimum temperature for preventing corrosion when the combustion residue (ash) contains approximately 3.5% vanadium. Indicates tube metal temperature.
この第1図よりも明かなごとく、媒体(給水)
の温度をこの曲線より高い処にする必要がある。 As is clearer from this Figure 1, the medium (water supply)
It is necessary to set the temperature to a point higher than this curve.
従来のボイラにおいてはこのような低温腐食を
防止するため給水温度を上昇させる手段として給
水加熱器又は加熱形脱気器を設けるなどしていた
が設備費が大きいものとなるという問題がある。 In conventional boilers, in order to prevent such low-temperature corrosion, a feed water heater or heating type deaerator is installed as a means to increase the feed water temperature, but there is a problem in that the equipment cost is high.
この発明は閣単な給水のバイパス管路と再循環
管路を主給水管路につき設けてこの問題を解決す
るものである。 The present invention solves this problem by providing a simple water supply bypass line and recirculation line for the main water supply line.
<発明の目的>
この発明はこのような低温腐食を生ずることな
くかつ既設のボイラにも適用でき、また管路等の
増設により容易にボイラ装置を改造でき、しかも
新設ボイラにおいては給水加熱器、加熱形脱気器
等を使用することなく節炭器の低温腐食を防止し
たボイラの構造を提案することを目的とする。<Purpose of the invention> The present invention can be applied to existing boilers without causing such low-temperature corrosion, and the boiler equipment can be easily modified by adding pipes, etc. Moreover, in new boilers, the feed water heater, The purpose of this study is to propose a boiler structure that prevents low-temperature corrosion of the economizer without using a heating type deaerator or the like.
<手段の概要>
要するにこの発明は、ボイラ給水ポンプ、主給
水流量制御弁、節炭器入口の給水温度発信器、節
炭器、節炭器出口の給水温度発信器、を主給水管
路の上流側より順に設けたボイラにおいて、給水
の一部を前記節炭器をバイパスしてボイラドラム
に供給する前記節炭器出口の温度発信器で制御さ
れるバイパス量調節弁付きの給水バイパス管路
と、再循環ポンプと前記節炭器入口の給水温度発
信器で制御される再循環流量調節弁とを有し前記
節炭器出口の給水の一部を前記節炭器の入口に供
給する給水再循環管路、とを設けたことを特徴と
するボイラ装置である。<Summary of Means> In short, the present invention provides a boiler feed pump, a main feed water flow rate control valve, a feed water temperature transmitter at the inlet of the economizer, a economizer, and a feed water temperature transmitter at the outlet of the economizer, in the main water supply pipe. In the boiler provided sequentially from the upstream side, a water supply bypass pipe line with a bypass amount adjustment valve controlled by a temperature transmitter at the outlet of the carbon economizer, which supplies a portion of the feed water to the boiler drum by bypassing the carbon economizer. and a recirculation pump and a recirculation flow control valve controlled by a feed water temperature transmitter at the inlet of the economizer, and a water supply supplying a portion of the feed water at the outlet of the economizer to the inlet of the economizer. This is a boiler device characterized by being provided with a recirculation pipe line.
<実施例>
第2図はこの発明の一実施例を示す管系統と制
御系統の図面である。この場合において、ボイラ
1への給水は給水タンク2より各部材を接続して
主給水系を形成する主給水管路3に順に設けたボ
イラ給水ポンプ4、主給水流量制御弁5、主給水
流量計6、節炭器7を経由しボイラの上胴1aに
供給される。主給水管路3は節炭器7の入口と給
水タンク2を接続する管路3aと節炭器出口と上
胴1aを接続する管路3bとよりなる。給水バイ
パス管路8にはバイパス量調節弁9を設け、給水
バイパス管路8の一端は管路3aと接続部8aで
接続し、他の一端は管路3bがドラム(上胴)入
口と接続する附近の接続部8bで接続する。<Embodiment> FIG. 2 is a diagram of a pipe system and a control system showing an embodiment of the present invention. In this case, water is supplied to the boiler 1 from a water supply tank 2 through a boiler feed pump 4, a main water flow rate control valve 5, and a main water flow rate, which are installed in order in a main water supply pipeline 3 that connects each member to form a main water supply system. A total of six fuels are supplied to the upper shell 1a of the boiler via the economizer 7. The main water supply conduit 3 consists of a conduit 3a that connects the inlet of the economizer 7 and the water supply tank 2, and a conduit 3b that connects the outlet of the economizer and the upper body 1a. The water supply bypass pipe 8 is provided with a bypass amount adjustment valve 9, one end of the water supply bypass pipe 8 is connected to the pipe 3a at a connecting part 8a, and the other end is connected to the drum (upper body) inlet by the pipe 3b. Connect at the nearby connecting part 8b.
また給水再循環路10は一端を給水流れについ
て接続部8aの下流で管路3aと接続部10aで
接続し、他の一端は接続部8bの管路3bについ
ての上流の接続部10bで接続する。この給水再
循環管路10には再循環ポンプ11と再循環量調
節弁12とが設けられる。燃焼ガスGはボイラ1
から煙道13経由節炭器7、に流れ給水と熱交換
しついで煙道14、煙突15を経由して排出され
る。 The feed water recirculation path 10 also has one end connected to the pipe 3a downstream of the connection 8a for the feed water flow at a connection 10a, and the other end connected to the connection 8b at the upstream connection 10b for the pipe 3b. . This water supply recirculation line 10 is provided with a recirculation pump 11 and a recirculation amount control valve 12 . Combustion gas G is boiler 1
The water flows through the flue 13 to the economizer 7, exchanges heat with the water supply, and is then discharged through the flue 14 and chimney 15.
このような装置において給水タンク2内の給水
はほぼ外気温度であり、仮りに15℃とすれば燃料
中の硫黄含有%に関係なく第1図から明らかな如
く節炭器の給水入口近傍伝熱管に低温腐食を起す
こととなる。 In such a device, the water supplied in the water supply tank 2 is at almost the outside temperature, and if the temperature is 15°C, the temperature of the heat exchanger tube near the water supply inlet of the economizer will increase regardless of the sulfur content in the fuel, as shown in Figure 1. This will cause low-temperature corrosion.
この場合に接続部8aから給水バイパス管路
8、バイパス量調節弁9を経由してバイパス給水
量を制御、従つて節炭器への給水量も制御すると
ともに、給水再循環管路10により節炭器7の出
口接続部10bより抽出する昇温した給水の一部
を再循環ポンプ11により昇圧し、その流量を再
循環流量調節弁12で制御して管路3aに供給す
ればこの昇温した給水と給水タンクからの給水と
混合し節炭器入口の給水温度を上昇させ低温腐食
を起さないものとすることができる。 In this case, the bypass water supply amount is controlled from the connection part 8a via the water supply bypass pipe line 8 and the bypass amount control valve 9, and therefore the water supply amount to the energy saver is also controlled, and the water supply recirculation line 10 is used to save water. This temperature increase can be achieved by increasing the pressure of a portion of the heated feed water extracted from the outlet connection part 10b of the coaler 7 by the recirculation pump 11, controlling its flow rate by the recirculation flow rate control valve 12, and supplying it to the pipe line 3a. By mixing the water supplied from the water supply tank with the water supplied from the water supply tank, the temperature of the water supply at the inlet of the economizer can be increased to prevent low-temperature corrosion.
さらに節炭器出口給水温度も制御されるため節
炭器出口給水温度がボイラの圧力に対する飽和温
度以下とすることができるため主給水管路にスチ
ーミングによる水槌現象(ウオータハンマ現象)
の生ずることを防ぐことができる。 Furthermore, since the temperature of the feed water at the outlet of the economizer is controlled, the temperature of the water feed water at the outlet of the economizer can be kept below the saturation temperature for the boiler pressure, resulting in the water hammer phenomenon caused by steaming in the main water supply pipe.
This can prevent the occurrence of
これらの各制御は排ガス温度計21からの信号
と、温度発信器16,18からの温度信号を記憶
と指令信号を出すボイラの主制御箱20によりさ
れる。この主制御箱20には負荷信号Lが送られ
ており、また主給水流量計6からの給水流量信号
も送られている。これらの信号を主制御箱でその
記憶数値と対比し主給水流量制御弁5、バイパス
量調節弁9、再循環流量調節弁12に指令信号が
送られそれぞれの流量調色がされる。 Each of these controls is performed by the boiler's main control box 20 which stores signals from the exhaust gas thermometer 21 and temperature signals from the temperature transmitters 16 and 18 and issues command signals. A load signal L is sent to this main control box 20, and a water supply flow rate signal from the main water supply flow meter 6 is also sent. These signals are compared with the stored values in the main control box, and command signals are sent to the main water supply flow rate control valve 5, the bypass amount control valve 9, and the recirculation flow rate control valve 12, and the respective flow rates are adjusted.
<発明の効果>
この発明を実施することにより給水のバイパス
量、再循環量が制御され節炭器入口給水の温度が
低温腐食メタル温度以上の適当な温度に制御され
節炭器の低温腐食を防止しかつウオータハンマ現
象を防止したボイラ装置とすることができるとい
う効果を奏する。<Effects of the Invention> By carrying out this invention, the bypass amount and recirculation amount of the feed water are controlled, and the temperature of the feed water at the inlet of the economizer is controlled to an appropriate temperature higher than the temperature of the low temperature corroding metal, thereby preventing low temperature corrosion of the economizer. This has the effect that it is possible to provide a boiler apparatus that prevents the water hammer phenomenon.
第1図は低温腐食を起さないための鋼管のメタ
ル温度と燃料中の硫黄含有量との関係を示す線
図、第2図は本発明にかかるボイラ装置の管系統
と制御系統を示す図面である。
1……ボイラ、3……主給水管路、3a,3b
……管路、8……給水バイパス管路、9……バイ
パス量調節弁、10……給水再循環管路、11…
…再循環ポンプ、12……再循環量調節弁、20
……主制御箱。
Fig. 1 is a diagram showing the relationship between the metal temperature of steel pipes and the sulfur content in the fuel to prevent low-temperature corrosion, and Fig. 2 is a drawing showing the pipe system and control system of the boiler equipment according to the present invention. It is. 1...Boiler, 3...Main water supply pipe, 3a, 3b
...Pipe line, 8... Water supply bypass pipe line, 9... Bypass amount control valve, 10... Water supply recirculation pipe line, 11...
... Recirculation pump, 12 ... Recirculation amount control valve, 20
...Main control box.
Claims (1)
器入口の給水温度発信器、節炭器、節炭器出口の
給水温度発信器、を主給水管路の上流側より順に
設けたボイラにおいて、給水の一部を前記節炭器
をバイパスしてボイラドラムに供給する前記節炭
器出口の温度発信器で制御されるバイパス量調節
弁付きの給水バイパス管路と、再循環ポンプと前
記節炭器入口の給水温度発信器で制御される再循
環流量調節弁とを有し前記節炭器出口の給水の一
部を前記節炭器の入口に供給する給水再循環管
路、とを設けたことを特徴とするボイラ装置。 2 記憶と指令信号を出すボイラの主制御箱に節
炭器入口排ガス温度、節炭器入口給水温度、節炭
器出口給水温度の信号を送り、かつボイラ負荷信
号と給水流量信号とを前記主制御箱に送り前記主
制御箱の記憶する値と対比して出す指令信号によ
りバイパス量調節弁と再循環量調節弁と主給水流
量制御弁とを制御し、節炭器伝熱管のメタル温度
を低温腐食を生ずる温度以上に保持可能にする主
制御箱と信号回路とを設けたことを特徴とする特
許請求の範囲第1項記載のボイラ装置。[Scope of Claims] 1. A boiler feed water pump, a main water supply flow rate control valve, a feed water temperature transmitter at the inlet of the economizer, a economizer, and a feed water temperature transmitter at the outlet of the economizer from the upstream side of the main water supply pipe. In the boilers provided in sequence, a feed water bypass pipe line with a bypass amount regulating valve controlled by a temperature transmitter at the outlet of the economizer, which supplies a part of the feed water to the boiler drum by bypassing the economizer; A feed water recirculation pipe having a circulation pump and a recirculation flow rate regulating valve controlled by a feed water temperature transmitter at the inlet of the economizer, and supplying a portion of the feed water at the outlet of the economizer to the inlet of the economizer. A boiler device characterized by being provided with a passage. 2. Send signals of the exhaust gas temperature at the inlet of the economizer, the water supply temperature at the inlet of the economizer, and the water supply temperature at the outlet of the economizer to the main control box of the boiler that outputs memory and command signals, and send the boiler load signal and the water supply flow rate signal to the main control box. The command signal sent to the control box and compared with the value stored in the main control box controls the bypass amount control valve, the recirculation amount control valve, and the main water supply flow rate control valve, and controls the metal temperature of the energy saver heat transfer tube. 2. The boiler device according to claim 1, further comprising a main control box and a signal circuit that can maintain the temperature at a temperature higher than that at which low-temperature corrosion occurs.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4461082A JPS58164907A (en) | 1982-03-23 | 1982-03-23 | Boiler device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4461082A JPS58164907A (en) | 1982-03-23 | 1982-03-23 | Boiler device |
Related Child Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP33097589A Division JPH02272205A (en) | 1989-12-19 | 1989-12-19 | Boiler device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS58164907A JPS58164907A (en) | 1983-09-29 |
| JPH0232525B2 true JPH0232525B2 (en) | 1990-07-20 |
Family
ID=12696208
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP4461082A Granted JPS58164907A (en) | 1982-03-23 | 1982-03-23 | Boiler device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS58164907A (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS60170502U (en) * | 1984-04-20 | 1985-11-12 | 三菱鉱業セメント株式会社 | Waste heat boiler equipment for cement firing equipment |
| US11420472B2 (en) | 2017-04-05 | 2022-08-23 | Nippon Steel Corporation | Front axle beam and production method thereof |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5888504U (en) * | 1981-12-11 | 1983-06-15 | 株式会社日立製作所 | Minimum flow control system |
-
1982
- 1982-03-23 JP JP4461082A patent/JPS58164907A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS58164907A (en) | 1983-09-29 |
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