JPS62162803A - Exhaust gas economizer - Google Patents

Exhaust gas economizer

Info

Publication number
JPS62162803A
JPS62162803A JP269886A JP269886A JPS62162803A JP S62162803 A JPS62162803 A JP S62162803A JP 269886 A JP269886 A JP 269886A JP 269886 A JP269886 A JP 269886A JP S62162803 A JPS62162803 A JP S62162803A
Authority
JP
Japan
Prior art keywords
water
exhaust gas
pressure
water supply
separator
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.)
Pending
Application number
JP269886A
Other languages
Japanese (ja)
Inventor
橋井 正昭
謙二 藤本
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.)
Mitsubishi Heavy Industries Ltd
Original Assignee
Mitsubishi 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 Mitsubishi Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP269886A priority Critical patent/JPS62162803A/en
Publication of JPS62162803A publication Critical patent/JPS62162803A/en
Pending legal-status Critical Current

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  • Control Of Steam Boilers And Waste-Gas Boilers (AREA)

Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明はディーゼル機関等の主機から排出される高温の
排ガスの熱を回収する排ガスエコノマイザ−に関する。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to an exhaust gas economizer that recovers heat from high-temperature exhaust gas discharged from a main engine such as a diesel engine.

〔従来の技術〕[Conventional technology]

第2図に従来の排ガスエコノマイザ−を示f。 FIG. 2 shows a conventional exhaust gas economizer.

低圧蒸気サービスシステム16及び高圧蒸気サービスシ
ステム17よりドレンとして回収された復水は、ドレン
タンク1に回収され、復水器2へ供給される。
Condensate collected as drain from the low pressure steam service system 16 and the high pressure steam service system 17 is collected in the drain tank 1 and supplied to the condenser 2.

一方1発電機タービン3よりの排気は、復水器2にて、
冷却水と熱交換を行い、冷却され復水となり、復水ポン
プ4により吸引され、給水ポンプ5に供給される。
On the other hand, the exhaust gas from the 1 generator turbine 3 is sent to the condenser 2.
It exchanges heat with the cooling water, is cooled, becomes condensate, is sucked by the condensate pump 4, and is supplied to the water supply pump 5.

他方、給水ポンプ5は低圧汽水分離器(又は低圧フラッ
シャ−)llよりのドレンを吸引し。
On the other hand, the water supply pump 5 sucks the drain from the low pressure brackish water separator (or low pressure flasher) 11.

更に高圧汽水分離器(又は高圧フラッンヤー)9からボ
イラー循環水ポンプ12により吸引されたボイラー水の
一部が温度調整弁14を経て、給水ポンプ5に供給され
る。
Furthermore, a portion of the boiler water sucked from the high-pressure brackish water separator (or high-pressure flanyard) 9 by the boiler circulation water pump 12 is supplied to the feed water pump 5 via the temperature control valve 14 .

温度調整弁14は給水ポンプ5の吐出側(又はり1ガス
エコノマイザ−6の一部を(14成している予頻・器7
の入口flli+ )の給水温度を検知し、同温変を規
定値に保持すべく開度が制御される。即ち温度調整弁1
4を通るボイラ水量が制御される。
The temperature control valve 14 is connected to the discharge side of the water supply pump 5 (or a part of the gas economizer 6).
The temperature of the water supply at the inlet fli+ is detected, and the opening degree is controlled to maintain the same temperature change at a specified value. That is, temperature adjustment valve 1
The amount of boiler water passing through 4 is controlled.

OFガスエコノマイザ一本体6内に配置された予熱器7
により、排ガスのエネルギーを吸収して高温度となった
給水は、高圧汽水分離器用給水制御弁8を経て、高圧汽
水分離器9及び低圧汽水分離器用給水制御弁10を経て
、低圧汽水分離器11に給水される。
OF gas economizer - preheater 7 arranged in main body 6
The feed water, which has become high in temperature by absorbing the energy of the exhaust gas, passes through the high-pressure brackish water separator water supply control valve 8, the high-pressure brackish water separator 9, the low-pressure brackish water separator water supply control valve 10, and then the low-pressure brackish water separator 11. is supplied with water.

高圧汽水分離器9に貯・えられたボイラー水はボイラー
水循環ポンプ12により排ガスエコマイザ一本体6内の
高圧蒸気発生器13により排ガスエネルギーを吸収し、
汽水混合体となって、高圧汽水分離器9に回収され、汽
水分離される。
The boiler water stored in the high-pressure brackish water separator 9 is used by the boiler water circulation pump 12 to absorb exhaust gas energy by the high-pressure steam generator 13 in the exhaust gas economizer body 6.
The brackish water mixture is collected in a high-pressure brackish water separator 9 and separated into brackish water.

高圧汽水分離器9内で分離された蒸気の一部は排ガスエ
コノマイザ一本体6内の過熱器15により排ガスエネル
ギーを吸収して過熱蒸気となり1発電機タービン3に供
給される。
A part of the steam separated in the high-pressure brackish water separator 9 absorbs exhaust gas energy by the superheater 15 in the exhaust gas economizer body 6 and becomes superheated steam, which is supplied to the generator turbine 3.

一方、高圧汽水分離器9から取出された蒸気の一部は高
圧蒸気サービスシステム17に供給される。
On the other hand, a part of the steam taken out from the high pressure steam separator 9 is supplied to the high pressure steam service system 17.

又、低圧汽水分離器11から取出された蒸気の一部は発
電機タービン8へ供給され、又一部は低圧蒸気サービス
システム16へ供給すれる。
Further, a part of the steam taken out from the low-pressure steam separator 11 is supplied to the generator turbine 8, and a part is supplied to the low-pressure steam service system 16.

〔発明が解決しようとする問題点〕[Problem that the invention seeks to solve]

排ガスエコノマイザ−の蒸気発生器の応力腐食割れの発
生等を防止する為に、高圧蒸気発生器13への給水量は
1通常発生蒸気量の5倍から8倍とする必要がある。(
即ち循環比を5〜8とする必要がある。) 従来の装置では、予熱器7への給水温度を規定の温度に
保持する為に、ボイラー水循環ポンプ12の吐出側より
、高温のボイラー水を低温の復水系へ戻しているが1発
電機タービン3の負荷変動や復水器2の冷却水の温度変
化などの外乱要因により、給水温度が変化するために、
温寒調整弁14の開度が一定とならず、開度が変動する
In order to prevent the occurrence of stress corrosion cracking in the steam generator of the exhaust gas economizer, the amount of water supplied to the high-pressure steam generator 13 needs to be 5 to 8 times the amount of steam normally generated. (
That is, it is necessary to set the circulation ratio to 5 to 8. ) In the conventional system, in order to maintain the water supply temperature to the preheater 7 at a specified temperature, high-temperature boiler water is returned to the low-temperature condensate system from the discharge side of the boiler water circulation pump 12, but one generator turbine Because the feed water temperature changes due to disturbance factors such as load fluctuations in 3 and changes in the temperature of the cooling water in condenser 2,
The opening degree of the temperature/cold adjustment valve 14 is not constant and varies.

即ちボイラー水循環ポンプ12による高圧蒸気発生器1
3への安定的循環水の供給が確保できず循環比を正しく
保持出来ないため、排ガスエコノマイザ一本体6内の高
圧蒸気発生器18への給水量不足による高圧蒸気発生器
13の応力腐食割れ等の事故の発生をうながすこととな
る。
That is, a high pressure steam generator 1 using a boiler water circulation pump 12
Since a stable supply of circulating water to 3 cannot be ensured and the circulation ratio cannot be maintained correctly, stress corrosion cracking of the high pressure steam generator 13 due to insufficient water supply to the high pressure steam generator 18 in the exhaust gas economizer body 6. This will encourage the occurrence of accidents.

〔問題点を解決するだめの手段〕[Failure to solve the problem]

本発明は、高圧蒸気発生器へのボイラー水の併給ぶ−を
減すことなく、給水温度を所定の値とする為に、高圧汽
水分離器中に設けた伝熱管内に復水の一部を流し、高温
水を発生させこれを給水系へ戻す系統を設けた排ガスエ
コノマイザ−を提供する。
In order to maintain the feed water temperature at a predetermined value without reducing the co-feeding of boiler water to the high-pressure steam generator, a portion of the condensate water is placed in a heat transfer tube installed in a high-pressure brackish water separator. To provide an exhaust gas economizer equipped with a system for flowing water, generating high-temperature water, and returning it to a water supply system.

〔作用〕[Effect]

予y、 Bに入る給水の@度が低いと復水の1部を高圧
汽水分)::器内の伝熱管に入れ、ここで復水を昇温し
て高温水とし、高温水を給水系に戻して混合して給水の
温度を上げる。
For example, if the temperature of the feed water entering B is low, part of the condensate is converted into high-pressure brackish moisture): A part of the condensate is put into a heat transfer tube in the vessel, where the temperature of the condensate is raised to make high-temperature water, and the high-temperature water is supplied as water. Mix it back into the system and raise the temperature of the feed water.

〔実施例〕〔Example〕

本発明を第1図に示す実施例に基づいて説明する。 The present invention will be explained based on the embodiment shown in FIG.

排ガスエコノマイザ一本体6内には、主機からの排ガス
流れ方向上流側から順に、過熱器15゜高圧蒸発器18
.及び、予熱器7が配置されている。予熱器7は途中に
高圧汽水分離器用給水制御弁8を具えた管により高圧汽
水分離器と連通ずるとともに、制御弁8の上流側の管か
ら分岐し、途中に低圧汽水分離器用給水制御弁10を具
えた管により低圧汽水分離器11に連通している。
Inside the exhaust gas economizer body 6, in order from the upstream side in the flow direction of exhaust gas from the main engine, there are a superheater 15° and a high pressure evaporator 18.
.. A preheater 7 is also arranged. The preheater 7 communicates with the high-pressure brackish water separator through a pipe having a water supply control valve 8 for the high-pressure brackish water separator in the middle, and branches from a pipe on the upstream side of the control valve 8, and has a water supply control valve 10 for the low-pressure brackish water separator in the middle. It communicates with a low-pressure brackish water separator 11 by a pipe equipped with.

低圧汽水分離器11の蒸気部は低圧蒸気サービスシステ
ム16と管を介して連通し、低圧蒸気サービスシステム
16で仕事をした後のドレンをドレンタンク1に供給す
る管が低圧蒸気サービスシステム16に連結されている
。又、低圧汽水分離器11の蒸気部は発電機タービン3
の途中とも連通している。高圧汽水分離器9のボイラー
水都は、途中にボイラー水循環ポンプ12を具えた管を
介して高圧蒸発器13の入口部と連通し、高圧蒸発器1
3の出口部は戻り管により高圧汽水分離器9と連通して
いる。高圧汽水分離器9の蒸気部は過熱器15の入口と
連通ずるとともに高圧蒸気サービスシステム17と連通
している。高圧蒸気サービスシステム17も又ドレンタ
ンク1と連通している。
The steam section of the low-pressure steam water separator 11 communicates with the low-pressure steam service system 16 via a pipe, and the pipe that supplies drain after work in the low-pressure steam service system 16 to the drain tank 1 is connected to the low-pressure steam service system 16. has been done. Furthermore, the steam section of the low pressure brackish water separator 11 is connected to the generator turbine 3.
It also communicates with the middle of the. The boiler water pipe of the high-pressure brackish water separator 9 communicates with the inlet of the high-pressure evaporator 13 via a pipe equipped with a boiler water circulation pump 12 in the middle.
The outlet portion of No. 3 communicates with a high-pressure brackish water separator 9 through a return pipe. The steam section of the high pressure steam separator 9 communicates with the inlet of the superheater 15 and also with the high pressure steam service system 17. A high pressure steam service system 17 is also in communication with the drain tank 1.

過熱器15の出口は発電機タービン8の入口と連通し1
発電機タービン3の出口は管を介して復水器2と連通し
ている。復水器2には、さらにドレンタンク1内のドレ
ンが導かれる管が連結している。り水部2の出口は途中
に復水ポンプを具えた給水管により給水ポンプ5の入口
部と連通している。低圧汽水分離器11の復水部の出口
に管が連結され、この復水管19は給水ポンプ5の入口
上流側の給水管に連結している。又。
The outlet of the superheater 15 communicates with the inlet of the generator turbine 8 1
The outlet of the generator turbine 3 communicates with the condenser 2 via a pipe. The condenser 2 is further connected to a pipe through which the drain in the drain tank 1 is guided. The outlet of the water supply section 2 communicates with the inlet of the water supply pump 5 through a water supply pipe equipped with a condensate pump in the middle. A pipe is connected to the outlet of the condensate part of the low-pressure brackish water separator 11, and this condensate pipe 19 is connected to a water supply pipe upstream of the inlet of the water supply pump 5. or.

復水管19は途中で分岐し高圧汽水分離器9内に配置さ
れたヒーティングコイル18の入口と連通し、さらにヒ
ーティングコイル18の出口は1度調整弁14を介して
復水管19に連結している。
The condensate pipe 19 branches in the middle and communicates with the inlet of a heating coil 18 disposed in the high-pressure brackish water separator 9, and the outlet of the heating coil 18 is once connected to the condensate pipe 19 via a regulating valve 14. ing.

給水ポンプ5の出口ml+は給水管を介して予熱器7の
入口と連通している。
The outlet ml+ of the water supply pump 5 communicates with the inlet of the preheater 7 via a water supply pipe.

高圧汽水分離器9から、ボイラー水循環ポンプ12によ
り吸引されたボイラー水は排ガスエコノマイザ一本体6
内の高圧蒸気発生器13により排ガス中の熱エネルギー
を吸収し、汽水混合体となり、高圧汽水分離器9へ戻さ
れる。
The boiler water sucked from the high-pressure brackish water separator 9 by the boiler water circulation pump 12 is transferred to the exhaust gas economizer body 6.
Thermal energy in the exhaust gas is absorbed by the high-pressure steam generator 13 in the exhaust gas to form a brackish water mixture, which is returned to the high-pressure brackish water separator 9.

一方、排ガスエコノマイザ一本体6内の予継器7の給水
の入口温度(又は給水ボンダ5の出口温度)は、低圧汽
水分離器11よりの復水の一部を高圧汽水分離器9中に
設けられた伝熱管であるヒーティングコイル18内を通
過させることによって得られた高温水を、温度調整弁1
4を介して復水の残り(ヒーティングコイル18を通ら
ない分)と混合することにより自動的に制御される。温
度調整弁14は予熱器7の入口(又は給水ポンプ5の吐
出側)温度を検出し、この温度が規定値となる様に高圧
汽水分離器9中に設けられたヒーティングコイル18内
を流れる復水の量を制御する機能を有する。
On the other hand, the inlet temperature of the feed water of the relay unit 7 in the exhaust gas economizer main body 6 (or the outlet temperature of the water supply bonder 5) is determined by directing a portion of the condensate from the low pressure brackish water separator 11 into the high pressure brackish water separator 9. The high temperature water obtained by passing through the heating coil 18, which is a heat transfer tube, is passed through the temperature adjustment valve 1.
4 and the rest of the condensate (the portion that does not pass through the heating coil 18). The temperature control valve 14 detects the temperature of the inlet of the preheater 7 (or the discharge side of the water supply pump 5), and the water flows through the heating coil 18 provided in the high-pressure brackish water separator 9 so that this temperature becomes a specified value. It has the function of controlling the amount of condensate.

〔発明の効果〕〔Effect of the invention〕

蒸気発生器へ送られるボイラー水の1部を抽出して混合
することなく、給水の温度制御ができるので高圧蒸気発
生器へ安定した量のボイラー水の供給が可能となり、高
圧蒸気発生器の応力腐食割れなど、蒸気発生器への循環
水量不足に伴なう諸問題を解決出来る。
Since the temperature of the feed water can be controlled without extracting and mixing a portion of the boiler water sent to the steam generator, it is possible to supply a stable amount of boiler water to the high pressure steam generator, reducing stress in the high pressure steam generator. It can solve various problems caused by insufficient amount of circulating water to the steam generator, such as corrosion cracking.

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

第1図は本発明の実施例の系統図、第2図は従来装置の
系統図である。 5・・・給水ポンプ、6・・・排ガスエコノマイザー不
休、7・・・予熱器、9・・・高圧汽水分離器、13・
・・高圧蒸気発生器、15・・・過熱器、18・・・ヒ
ーティングコイル 晃1図
FIG. 1 is a system diagram of an embodiment of the present invention, and FIG. 2 is a system diagram of a conventional device. 5... Water supply pump, 6... Exhaust gas economizer, 7... Preheater, 9... High pressure brackish water separator, 13...
...High pressure steam generator, 15... Superheater, 18... Heating coil Ko 1 diagram

Claims (1)

【特許請求の範囲】[Claims] 排ガスエコノマイザ本体内に主機排ガス流れ方向の上流
側から順に過熱器、高圧蒸気発生器、予熱器が配置され
、前記予熱器出口が高圧汽水分離器に連通し、給水ポン
プ上流側に復水が流れる給水管を連結し、前記給水ポン
プ出口が給水管を介して前記予熱器入口を連通し、前記
高圧汽水分離器の高温水部と前記高圧蒸気発生器とを循
環系統で連通し、前記高圧汽水分離器の蒸気部と前記過
熱器の入口部とを連通した排ガスエコノマイザにおいて
、前記高圧汽水分離器内に伝熱管を配置し、同伝熱管に
復水の一部を導びいて前記給水ポンプ上流側の給水管に
供給する系統を設けたことを特徴とする排ガスエコノマ
イザ。
A superheater, a high-pressure steam generator, and a preheater are arranged in the exhaust gas economizer body in order from the upstream side in the main engine exhaust gas flow direction, the outlet of the preheater communicates with the high-pressure brackish water separator, and condensate flows to the upstream side of the water supply pump. water supply pipes are connected, the water supply pump outlet communicates with the preheater inlet via the water supply pipe, the high-temperature water section of the high-pressure brackish water separator and the high-pressure steam generator are connected through a circulation system, and the high-pressure brackish water In an exhaust gas economizer that communicates the steam section of the separator with the inlet of the superheater, a heat transfer tube is disposed in the high-pressure brackish water separator, and a portion of the condensate is guided to the heat transfer tube upstream of the feed water pump. An exhaust gas economizer characterized by having a system for supplying water to the side water supply pipe.
JP269886A 1986-01-09 1986-01-09 Exhaust gas economizer Pending JPS62162803A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP269886A JPS62162803A (en) 1986-01-09 1986-01-09 Exhaust gas economizer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP269886A JPS62162803A (en) 1986-01-09 1986-01-09 Exhaust gas economizer

Publications (1)

Publication Number Publication Date
JPS62162803A true JPS62162803A (en) 1987-07-18

Family

ID=11536497

Family Applications (1)

Application Number Title Priority Date Filing Date
JP269886A Pending JPS62162803A (en) 1986-01-09 1986-01-09 Exhaust gas economizer

Country Status (1)

Country Link
JP (1) JPS62162803A (en)

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