JPH0322521B2 - - Google Patents

Info

Publication number
JPH0322521B2
JPH0322521B2 JP59139453A JP13945384A JPH0322521B2 JP H0322521 B2 JPH0322521 B2 JP H0322521B2 JP 59139453 A JP59139453 A JP 59139453A JP 13945384 A JP13945384 A JP 13945384A JP H0322521 B2 JPH0322521 B2 JP H0322521B2
Authority
JP
Japan
Prior art keywords
temperature
economizer
water
boiler
waste heat
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
Application number
JP59139453A
Other languages
Japanese (ja)
Other versions
JPS6117804A (en
Inventor
Shunpei Nozoe
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Kawasaki Heavy Industries Ltd
Original Assignee
Kawasaki Heavy Industries Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Kawasaki Heavy Industries Ltd filed Critical Kawasaki Heavy Industries Ltd
Priority to JP13945384A priority Critical patent/JPS6117804A/en
Publication of JPS6117804A publication Critical patent/JPS6117804A/en
Publication of JPH0322521B2 publication Critical patent/JPH0322521B2/ja
Granted legal-status Critical Current

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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) 本発明は、エコノマイザの腐食の問題を解決
し、廃熱を効率よく回収するようにした廃熱ボイ
ラに関する。
DETAILED DESCRIPTION OF THE INVENTION (Industrial Application Field) The present invention relates to a waste heat boiler that solves the problem of economizer corrosion and efficiently recovers waste heat.

(従来技術とその問題点) 従来、廃熱ボイラに於いて、特に硫黄分を多量
に含んでいる排ガスは、腐食の問題があるので、
低温域での熱回収は行なわれずそのまゝ放散して
いた。
(Prior art and its problems) Conventionally, in waste heat boilers, the exhaust gas containing a particularly large amount of sulfur has a problem of corrosion.
Heat was not recovered in the low temperature range and was dissipated as is.

即ち、第3図に示すように、従来の廃熱ボイラ
は、ボイラ給水ポンプ3による給水をエコノマイ
ザ4に導いて昇温し、ボイラドラム1に給水す
る。この給水されたボイラドラム1内の給水は、
蒸発器5によつて、廃熱を収熱し、蒸発する。こ
の蒸気は、更に最も高温側に設けられたスーパヒ
ータ6に導かれ、過熱蒸気となる。
That is, as shown in FIG. 3, in the conventional waste heat boiler, the water supplied by the boiler feed water pump 3 is guided to the economizer 4, where the temperature is raised, and the water is supplied to the boiler drum 1. This water supply inside the boiler drum 1 is as follows:
The evaporator 5 collects waste heat and evaporates it. This steam is further guided to the superheater 6 provided on the highest temperature side, and becomes superheated steam.

この従来の廃熱ボイラにおいて、廃熱温度が低
い場合は、最低温部に配設されたエコノマイザ4
の管壁温度が低下し、廃ガス中に含まれている硫
黄分の露点以下まで低下すると、エコノマイザ4
は腐食し、実質上廃熱ボイラの運転が不可能とな
る。
In this conventional waste heat boiler, when the waste heat temperature is low, the economizer 4 installed in the lowest temperature part
When the pipe wall temperature of the economizer 4 decreases to below the dew point of the sulfur contained in the waste gas,
is corroded, making it virtually impossible to operate the waste heat boiler.

従つて、エコノマイザが腐食するような低温域
での熱回収はエコノマイザ4を設置しないでその
まま放熱するか、又は別置の給水ヒータ15で給
水予熱を行つているのが実情である。
Therefore, in order to recover heat in a low temperature range where the economizer is corroded, the actual situation is to simply dissipate the heat without installing the economizer 4, or to preheat the water supply using a separately installed water heater 15.

(発明の目的) 本発明は、上記実情に鑑みなされたものであ
り、エコノマイザの腐食の問題を解決し、低温域
での廃熱回収を効率良く行うようにした廃熱ボイ
ラを提供せんとするものである。
(Objective of the Invention) The present invention has been made in view of the above circumstances, and aims to provide a waste heat boiler that solves the problem of economizer corrosion and efficiently recovers waste heat in a low temperature range. It is something.

(発明の構成) 本発明は、ボイラ給水ポンプからの給水をエコ
ノマイザにて昇温し、この昇温した給水を蒸発器
に導いて蒸発させ、この蒸発をスーパヒータに導
いて過熱蒸気を得るようにした廃熱ボイラにおい
て、蒸発器の高温水の一部をエコノマイザ給水入
口に合流し、エコノマイザ入口給水温度を制御す
るようにしたことを特徴とする。
(Structure of the Invention) The present invention raises the temperature of feed water from a boiler feed water pump using an economizer, leads the heated feed water to an evaporator to be evaporated, and leads the evaporation to a superheater to obtain superheated steam. The waste heat boiler is characterized in that a part of the high temperature water of the evaporator flows into the economizer water supply inlet to control the temperature of the economizer inlet water supply.

(実施例) 本発明による廃熱ボイラの一実施例を第1図に
よつて説明する。図中第3図と同一符号は同一物
を示しており、給水ポンプ3からの給水はエコノ
マイザ4により昇温され、ボイラドラム1に給水
され、蒸発器5にて昇温されて蒸発し、更にスー
パヒータ6にて過熱蒸気になされることは従来の
廃熱ボイラと同一構成である。本発明の廃熱ボイ
ラは、この他水ドラム2よりエコノマイザ4への
給水管7に配管8を接続し、この配管8の途中に
循環ポンプ9、温度制御弁10を設け、温度制御
弁10をエコノマイザ4の入口部に設けた温度検
出器11の検出温度により開閉制御するようにし
てある。尚12は給水流量調節弁で、これはドラ
ム水位計16の信号の一要素制御又はドラム水位
計16、蒸気流量計14及び給水流量計17の各
信号を演算器18で演算した信号による三要素制
御のいずれかにより制御されるようになつてい
る。
(Example) An example of a waste heat boiler according to the present invention will be described with reference to FIG. In the figure, the same reference numerals as in FIG. 3 indicate the same parts, and the water supplied from the water supply pump 3 is heated by the economizer 4, supplied to the boiler drum 1, heated by the evaporator 5 and evaporated, and then What is done to the superheated steam in the superheater 6 is the same as that of a conventional waste heat boiler. In addition, in the waste heat boiler of the present invention, a piping 8 is connected to a water supply pipe 7 from the water drum 2 to an economizer 4, and a circulation pump 9 and a temperature control valve 10 are installed in the middle of this piping 8. Opening/closing control is performed based on the temperature detected by a temperature detector 11 provided at the inlet of the economizer 4. Reference numeral 12 denotes a water supply flow rate control valve, which controls one element of the signal from the drum water level gauge 16 or controls three elements based on signals calculated by a calculator 18 from the signals of the drum water level gauge 16, steam flow meter 14, and water supply flow meter 17. control.

(作用) かように構成された上記実施例の廃熱ボイラに
於いて、給水ポンプ3からエコノマイザ4への給
水量は、前述のように一要素又は三要素制御によ
り開度が制御される給水流量調節弁12により調
節される。一方温度調節用として水ドラム2より
取り出した高温水は配管8、給水管7を経て再び
エコノマイザ4に戻るので、ボイラ内を循環する
ことになり、ボイラ内の保有給水量は変らず、従
つて給水流量調節弁12に対する流量には影響し
ない。
(Function) In the waste heat boiler of the above embodiment configured as described above, the amount of water supplied from the water supply pump 3 to the economizer 4 is determined by the water supply whose opening degree is controlled by one-element or three-element control as described above. It is regulated by a flow rate control valve 12. On the other hand, the high-temperature water taken out from the water drum 2 for temperature adjustment returns to the economizer 4 again via piping 8 and water supply pipe 7, so it circulates within the boiler, and the amount of water supplied within the boiler does not change. The flow rate to the water supply flow rate control valve 12 is not affected.

さてエコノマイザ4の管壁温度は、次のように
して調整される。即ち、エコノマイザ4の管壁温
度は、その内部を流れる給水温度によつて理論的
に求められる。従つてエコノマイザ4の入口給水
温度を調節することにより、間接的にその管壁温
度が調節される。
Now, the tube wall temperature of the economizer 4 is adjusted as follows. That is, the tube wall temperature of the economizer 4 is theoretically determined by the temperature of the water supply flowing inside it. Therefore, by adjusting the inlet water temperature of the economizer 4, the tube wall temperature is indirectly adjusted.

エコノマイザ4を入口給水温度を、温度検出器
11により検出し、温度制御弁10の開度を調節
し、エコノマイザ4の管壁温度が、廃ガス中の硫
黄分の露点温度以上になるように、エコノマイザ
4の給水入口温度を調節する。
The inlet water temperature of the economizer 4 is detected by the temperature detector 11, and the opening degree of the temperature control valve 10 is adjusted so that the pipe wall temperature of the economizer 4 is equal to or higher than the dew point temperature of the sulfur content in the waste gas. Adjust the water supply inlet temperature of economizer 4.

この場合、水ドラム2からの注水は、エコノマ
イザ4への給水温度を昇温するためにのみ使用さ
れるので、外部への放熱はなく、エコノマイザ4
の腐食を防止しながら、低温域での廃熱を効率よ
く回収することになる。
In this case, the water injected from the water drum 2 is used only to raise the temperature of the water supplied to the economizer 4, so no heat is radiated to the outside, and the water is supplied to the economizer 4.
This will efficiently recover waste heat at low temperatures while preventing corrosion.

尚第2図は、強制循環ボイラに適用した場合の
他の実施例であり、ボイラ給水ポンプ3により給
水された水は、エコノマイザ4にて昇温され蒸気
ドラム1に給水される。この給水は、循環ポンプ
9により蒸発器5に導かれて蒸発し、蒸気ドラム
1に入り、次いでスーパヒータ6にて過熱され
る。
FIG. 2 shows another embodiment in which the system is applied to a forced circulation boiler, in which water supplied by a boiler feed water pump 3 is heated in an economizer 4 and supplied to a steam drum 1. This feed water is guided to the evaporator 5 by the circulation pump 9, evaporated, enters the steam drum 1, and then superheated by the super heater 6.

エコノマイザ4の給水入口温度は、温度検出器
11によつて検出され、これにより温度制御弁1
0の開度を調節し、循環ポンプ9からの分流量に
よつて、同様にエコノマイザ4の管壁温度が調整
される。
The feed water inlet temperature of the economizer 4 is detected by the temperature detector 11, and the temperature control valve 1 is thereby detected.
Similarly, the tube wall temperature of the economizer 4 is adjusted by adjusting the opening degree of 0 and the divided flow rate from the circulation pump 9.

この実施例においても、温度調節用の高温水
は、ボイラ内を循環するので、給水流量調節弁1
2の流量制御には影響しないこと、又蒸発器5か
ら取出される高温水は、給水の昇温にのみ使用さ
れて外部への放熱はなく、低温域における廃熱を
効率よく回収する点については、第1図に示す実
施例と同じである。
In this embodiment as well, since the high temperature water for temperature adjustment circulates within the boiler, the water supply flow rate control valve 1
Regarding the fact that it does not affect the flow rate control in step 2, and that the high temperature water taken out from the evaporator 5 is used only to raise the temperature of the feed water and does not radiate heat to the outside, it efficiently recovers waste heat in the low temperature range. is the same as the embodiment shown in FIG.

(発明の効果) 以上詳述した通り、本発明による廃熱ボイラ
は、蒸発器から一部の高温水を分岐して、エコノ
マイザの給水入口に注水し、エコノマイザ入口の
給水温度を調節するようにしたので、エコノマイ
ザの管壁温度を廃ガス中の硫黄分の露点温度以上
にできて、管壁の腐食を防止できしかも低温域に
おける廃ガスの熱回収が可能となるなどの優れた
効果がある。
(Effects of the Invention) As detailed above, the waste heat boiler according to the present invention branches some high-temperature water from the evaporator and injects it into the water supply inlet of the economizer to adjust the temperature of the water supply at the economizer inlet. As a result, the temperature of the economizer tube wall can be made higher than the dew point temperature of the sulfur content in the waste gas, which has excellent effects such as preventing corrosion of the tube wall and making it possible to recover heat from the waste gas at low temperatures. .

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

第1図及び第2図は本発明の一実施例であり、
第1図は自然循環ボイラに適用した場合を、第2
図は強制循環ボイラに適用した場合のフローシー
トである。第3図は自然循環ボイラを例に示した
従来の廃熱ボイラのフローシートである。 1……蒸気ドラム、2……水ドラム、3……給
水ポンプ、4……エコノマイザ、5……蒸発器、
6……スーパヒータ、7……給水管、8……配
管、9……循環ポンプ、10……温度制御弁、1
1……温度検出器、12……給水流量調節弁、1
3……出口管、14……流量検出器、15……給
水ヒータ、16……ドラム水位計、17……給水
流量計、18……演算器。
FIG. 1 and FIG. 2 are one embodiment of the present invention,
Figure 1 shows the case where it is applied to a natural circulation boiler.
The figure is a flow sheet when applied to a forced circulation boiler. FIG. 3 is a flow sheet of a conventional waste heat boiler, taking a natural circulation boiler as an example. 1...Steam drum, 2...Water drum, 3...Water pump, 4...Economizer, 5...Evaporator,
6... Super heater, 7... Water supply pipe, 8... Piping, 9... Circulation pump, 10... Temperature control valve, 1
1...Temperature detector, 12...Water supply flow rate control valve, 1
3... Outlet pipe, 14... Flow rate detector, 15... Water supply heater, 16... Drum water level gauge, 17... Water supply flow meter, 18... Arithmetic unit.

Claims (1)

【特許請求の範囲】[Claims] 1 ボイラ給水ポンプからの給水をエコノマイザ
にて昇温し、この昇温した給水を蒸発器に導いて
蒸発させ、この蒸気をスーパヒータに導いて過熱
蒸気を得るようにした廃熱ボイラにおいて、蒸発
器の高温水の一部をエコノマイザ給水入口に合流
し、エコノマイザ入口給水温度を制御するように
したことを特徴とする廃熱ボイラ。
1 In a waste heat boiler in which the feed water from the boiler feed water pump is heated by an economizer, this heated feed water is led to an evaporator to be evaporated, and this steam is led to a superheater to obtain superheated steam, the evaporator A waste heat boiler characterized in that a part of the high-temperature water is merged into an economizer water supply inlet to control the temperature of the economizer inlet water supply.
JP13945384A 1984-07-05 1984-07-05 Waste heat boiler Granted JPS6117804A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP13945384A JPS6117804A (en) 1984-07-05 1984-07-05 Waste heat boiler

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP13945384A JPS6117804A (en) 1984-07-05 1984-07-05 Waste heat boiler

Publications (2)

Publication Number Publication Date
JPS6117804A JPS6117804A (en) 1986-01-25
JPH0322521B2 true JPH0322521B2 (en) 1991-03-27

Family

ID=15245561

Family Applications (1)

Application Number Title Priority Date Filing Date
JP13945384A Granted JPS6117804A (en) 1984-07-05 1984-07-05 Waste heat boiler

Country Status (1)

Country Link
JP (1) JPS6117804A (en)

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6047481B2 (en) * 1979-04-10 1985-10-22 三井造船株式会社 Internal combustion engine exhaust gas heat recovery method and device

Also Published As

Publication number Publication date
JPS6117804A (en) 1986-01-25

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