[go: up one dir, main page]

JPH074263A - Regeneration cycle gas turbine equipment using steam - Google Patents

Regeneration cycle gas turbine equipment using steam

Info

Publication number
JPH074263A
JPH074263A JP14329393A JP14329393A JPH074263A JP H074263 A JPH074263 A JP H074263A JP 14329393 A JP14329393 A JP 14329393A JP 14329393 A JP14329393 A JP 14329393A JP H074263 A JPH074263 A JP H074263A
Authority
JP
Japan
Prior art keywords
steam
compressor
air
regenerator
turbine
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
JP14329393A
Other languages
Japanese (ja)
Inventor
Jube Matsumura
重兵衛 松村
Shizuka Mizuno
静 水野
Akira Hirano
昭 平野
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.)
Hitachi Ltd
Hitachi Industry and Control Solutions Co Ltd
Original Assignee
Hitachi Engineering Co Ltd Ibaraki
Hitachi 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 Hitachi Engineering Co Ltd Ibaraki, Hitachi Ltd filed Critical Hitachi Engineering Co Ltd Ibaraki
Priority to JP14329393A priority Critical patent/JPH074263A/en
Publication of JPH074263A publication Critical patent/JPH074263A/en
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E20/00Combustion technologies with mitigation potential
    • Y02E20/16Combined cycle power plant [CCPP], or combined cycle gas turbine [CCGT]

Landscapes

  • Engine Equipment That Uses Special Cycles (AREA)

Abstract

(57)【要約】 (修正有) 【構成】ボイラ給水33は、熱交換器15で圧縮機から
抽出空気と熱交換し、排熱回収ボイラ22に入る。発生
した蒸気34は、再生器蒸気ライン39で蒸気供給制御
弁38を通り、再生器51に入り圧縮機吐出空気を加熱
する。 【効果】タービンの冷却空気を作る設備が無くなるの
で、消費動力が減り、圧縮機の抽出空気の熱をボイラ給
水に与え蒸気の蒸発量を増やし、発生した蒸気が余る時
に再生器へ送り燃焼用空気を加熱することにより、プラ
ントの熱効率を向上させる。
(57) [Summary] (Correction) [Constitution] The boiler feed water 33 exchanges heat with the extracted air from the compressor in the heat exchanger 15, and enters the exhaust heat recovery boiler 22. The generated steam 34 passes through the steam supply control valve 38 in the regenerator steam line 39, enters the regenerator 51, and heats the compressor discharge air. [Effect] Since there is no facility for producing cooling air for the turbine, the power consumption is reduced, the heat of the air extracted from the compressor is applied to the boiler feed water to increase the amount of steam evaporation, and when the generated steam is left, it is sent to the regenerator for combustion. Heating the air improves the thermal efficiency of the plant.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は蒸気利用再生サイクルガ
スタービン設備に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a steam utilization regeneration cycle gas turbine facility.

【0002】[0002]

【従来の技術】従来の技術を図1を用いて説明する。圧
縮機2は吸気ダクト1を通して大気を吸込み圧縮する
が、圧力が上昇した圧縮機吐出空気は温度も上昇して、
圧縮機出口ダクト3で燃焼器4に流入する。ここで燃料
5と混合し燃焼して1000℃以上の高温ガスとなり、
タービン入口ダクト6によりタービン11に入り回転動
力を発生する。この回転動力は圧縮機2と負荷12をシ
ャフト20で回転させる。タービンは高温ガスより金属
を守るため、冷却空気14を使用するのが、圧縮機の抽
出空気13は約200℃と温度が高いので、冷却水16
を熱交換器15に導入して吐出空気を冷やして冷却空気
14とする。熱交換器を出た冷却水19はラジエータ1
8により大気へ放熱し温度を下げて、循環水ポンプ17
により再び熱交換器に送られる。タービンを出た排気ガ
スはタービン出口ダクト21により排熱回収ボイラ22
に入り、給水タンク31から給水ポンプ32でボイラに
送られるボイラ給水33を加熱することにより蒸気34
を作る。一方、排気ガスは、排気ダクト23により煙突
41に入り大気へ放出される。蒸気はプロセス蒸気ライ
ン37で工場の各種加熱源として利用するが、通常夏場
は室の暖房が不要であり、被加熱品も大気で温度が上昇
しているので蒸気の必要量は、冬場より減少する。この
ため、大気放出ライン35に放出量を制御する蒸気放出
制御弁36を設け、発生した蒸気が余る時、このライン
を通して大気に放出する。これでは排熱を回収し熱効率
を向上させるメリットが完全に生かされない。
2. Description of the Related Art A conventional technique will be described with reference to FIG. The compressor 2 draws in and compresses the atmosphere through the intake duct 1, but the compressor discharge air whose pressure has risen also rises in temperature,
It flows into the combustor 4 at the compressor outlet duct 3. Here, it mixes with the fuel 5 and burns into a high temperature gas of 1000 ° C or higher,
The turbine inlet duct 6 enters the turbine 11 to generate rotational power. This rotational power causes the compressor 2 and the load 12 to rotate on the shaft 20. The turbine uses the cooling air 14 in order to protect the metal from the hot gas, but the extraction air 13 of the compressor has a high temperature of about 200 ° C., so the cooling water 16
Is introduced into the heat exchanger 15 to cool the discharge air to form the cooling air 14. The cooling water 19 exiting the heat exchanger is the radiator 1
8 radiates heat to the atmosphere to lower the temperature, and the circulating water pump 17
Is sent again to the heat exchanger. Exhaust gas from the turbine is exhausted by the turbine outlet duct 21 into an exhaust heat recovery boiler 22.
Steam from the water supply tank 31 by heating the boiler water supply 33 sent to the boiler by the water supply pump 32.
make. On the other hand, the exhaust gas enters the chimney 41 by the exhaust duct 23 and is discharged to the atmosphere. The steam is used as various heating sources in the factory on the process steam line 37, but usually the room does not need to be heated in the summer, and the temperature of the heated product also rises in the atmosphere, so the amount of steam required is less than in the winter. To do. For this reason, a steam discharge control valve 36 for controlling the discharge amount is provided in the atmosphere discharge line 35, and when the generated steam remains, it is discharged to the atmosphere through this line. With this, the merit of recovering the exhaust heat and improving the thermal efficiency cannot be fully utilized.

【0003】本排熱回収発電装置に関連した発明として
特開昭60−205102号公報が有るが、蓄熱槽や蒸発器を設
けているので設備費が高く、熱効率が悪い欠点が有る。
Japanese Patent Laid-Open No. 60-205102 discloses an invention related to this exhaust heat recovery power generator, but since it has a heat storage tank and an evaporator, it has the drawbacks of high equipment cost and poor thermal efficiency.

【0004】[0004]

【発明が解決しようとする課題】排熱回収発電設備の熱
効率は、供給される燃料の熱量を無駄なく利用すること
に有るが、従来はせっかく加熱された空気や蒸気の熱源
を有効利用していない。本発明の目的は、圧縮機で昇温
した空気から熱を回収すると共に、発生した蒸気を年間
を通して全部有効に利用することにある。
The thermal efficiency of the exhaust heat recovery power generation facility is to utilize the heat quantity of the supplied fuel without waste, but conventionally, the heat source of air or steam heated at all has been effectively used. Absent. An object of the present invention is to recover heat from the air heated by the compressor and to effectively utilize the generated steam all year round.

【0005】[0005]

【課題を解決するための手段】冷却空気として使うため
圧縮機抽出空気をボイラ給水で冷却し、逆にボイラ給水
を加熱する熱交換器を設ける。又、発生した蒸気を工場
内の加熱源として使用するラインと圧縮機出口ダクト3
に再生器を設け、これに蒸気を供給するラインを設け
る。
There is provided a heat exchanger for cooling the compressor extraction air with boiler feed water for use as cooling air, and conversely heating the boiler feed water. Also, the line that uses the generated steam as a heating source in the factory and the compressor outlet duct 3
A regenerator is installed in the room, and a line for supplying steam is installed in the regenerator.

【0006】[0006]

【作用】熱交換器で加熱したボイラ給水を排熱回収ボイ
ラに送れば従来より蒸気の発生量が増える。発生した蒸
気を工場内の加熱源として使用しない時には再生器に蒸
気を送り燃焼器の入口空気温度を上げることにより、燃
料供給量が減り熱効率が上昇する。
[Operation] If the boiler feed water heated by the heat exchanger is sent to the exhaust heat recovery boiler, the amount of steam generated will increase compared to the conventional case. When the generated steam is not used as a heating source in the factory, the steam is sent to the regenerator to raise the inlet air temperature of the combustor, thereby reducing the fuel supply amount and increasing the thermal efficiency.

【0007】[0007]

【実施例】以下、本発明の実施例を図2を用いて、詳細
に説明する。給水タンク31から給水ポンプ32で加圧
されたボイラ給水33は、熱交換器15で圧縮機の抽出
空気13により加熱され、排熱回収ボイラ22に入り蒸
気34を発生する。従来、この抽出空気が持っていた熱
量は大気に捨ていたが、ボイラ給水で回収することによ
りボイラでの蒸発量が増える。発生蒸気量が増えてもプ
ロセス蒸気ライン37で常に全量使用しなければ、熱効
率は向上しない。しかし、夏場はどうしても冬場より蒸
気使用量が減るので、これを捨てること無く有効に利用
するため、圧縮機出口ダクト3の途中に再生器51と再
生器蒸気ライン39及び蒸気供給制御弁38を設け、蒸
気を送ることにより燃焼器4に流入する圧縮機吐出空気
を加熱する。燃焼器は燃料5を注入して1000℃以上
のある一定温度の燃焼ガスを作るが、再生器で空気の温
度を上昇させているので、注入する燃料の消費量は通常
より少なくなる。このため、年間をとうして発生した蒸
気を全量有効に使用することが可能になり、常時最高の
熱効率でプラントを運転することが出来る。
Embodiments of the present invention will be described in detail below with reference to FIG. The boiler feed water 33 pressurized from the feed water tank 31 by the feed water pump 32 is heated by the extraction air 13 of the compressor in the heat exchanger 15, and enters the exhaust heat recovery boiler 22 to generate steam 34. Conventionally, the amount of heat that this extracted air had was discarded into the atmosphere, but the amount of evaporation in the boiler increases by recovering it with boiler feed water. Even if the amount of generated steam increases, the thermal efficiency cannot be improved unless the process steam line 37 always uses the entire amount. However, since the amount of steam used in summer is inevitably smaller than in winter, in order to use this effectively without discarding it, a regenerator 51, a regenerator steam line 39 and a steam supply control valve 38 are provided in the middle of the compressor outlet duct 3. , The compressor discharge air flowing into the combustor 4 is heated by sending steam. The combustor injects the fuel 5 to produce combustion gas at a certain constant temperature of 1000 ° C. or higher, but since the temperature of the air is raised in the regenerator, the consumption of the injected fuel becomes smaller than usual. For this reason, it becomes possible to effectively use the entire amount of steam generated over the course of the year, and it is possible to always operate the plant with the highest thermal efficiency.

【0008】もし、工場の各種加熱用として全量蒸気を
使う場合には、蒸気供給制御弁を閉じれば良く、両方に
蒸気を送る場合には蒸気供給制御弁を全閉/全開の途中
の開度とする。
If the full amount of steam is used for various heating in the factory, the steam supply control valve may be closed, and if steam is sent to both, the steam supply control valve is opened / closed during opening. And

【0009】[0009]

【発明の効果】本発明によれば、圧縮機の抽出空気を冷
却しタービンの冷却空気を作る設備を有していたが、ボ
イラ給水で代用するため、循環水ポンプとラジエータが
無くなり、設備費と消費動力が低減出来る。
According to the present invention, the equipment for cooling the extracted air of the compressor to produce the cooling air of the turbine was provided, but since the boiler water supply is used as a substitute, the circulating water pump and the radiator are eliminated, and the equipment cost is reduced. And the power consumption can be reduced.

【0010】また、圧縮機の抽出空気が保有している熱
量の一部を、ボイラ給水に与え排熱回収ボイラに送るの
で、蒸気の発生量が増える。
Further, since a part of the heat quantity held by the extracted air of the compressor is given to the boiler feed water and sent to the exhaust heat recovery boiler, the amount of steam generated increases.

【0011】さらに、排熱回収ボイラで発生した蒸気が
一部又は全部余る場合、従来大気に放出していたものを
再生器に送り、燃焼用空気である圧縮機吐出空気を加熱
し、燃焼器に注入される燃料消費量を減らし、熱効率が
向上する。
Further, when a part or all of the steam generated in the exhaust heat recovery boiler is surplus, what is conventionally discharged to the atmosphere is sent to the regenerator to heat the compressor discharge air which is the combustion air to heat the combustor. It reduces the fuel consumption injected into and improves thermal efficiency.

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

【図1】従来技術の排熱回収発電設備の全体系統図。FIG. 1 is an overall system diagram of a conventional exhaust heat recovery power generation facility.

【図2】本発明による蒸気利用再生サイクルガスタービ
ン設備の全体系統図。
FIG. 2 is an overall system diagram of a steam utilization regeneration cycle gas turbine facility according to the present invention.

【符号の説明】 1…吸気ダクト、2…圧縮機、3…圧縮機出口ダクト、
4…燃焼器、5…燃料、6…タービン入口ダクト、11
…タービン、12…負荷、13…抽出空気、14…冷却
空気、15…熱交換器、20…シャフト、21…タービ
ン出口ダクト、22…排熱回収ボイラ、23…排気ダク
ト、31…給水タンク、32…給水ポンプ、33…ボイ
ラ給水、34…蒸気、37…プロセス蒸気ライン、38
…蒸気供給制御弁、39…再生器蒸気ライン。
[Explanation of Codes] 1 ... Intake duct, 2 ... Compressor, 3 ... Compressor outlet duct,
4 ... Combustor, 5 ... Fuel, 6 ... Turbine inlet duct, 11
... turbine, 12 ... load, 13 ... extraction air, 14 ... cooling air, 15 ... heat exchanger, 20 ... shaft, 21 ... turbine exit duct, 22 ... exhaust heat recovery boiler, 23 ... exhaust duct, 31 ... water tank, 32 ... Water supply pump, 33 ... Boiler water supply, 34 ... Steam, 37 ... Process steam line, 38
… Steam supply control valve, 39… Regenerator steam line.

フロントページの続き (72)発明者 平野 昭 茨城県日立市幸町三丁目2番1号 日立エ ンジニアリング株式会社内Front Page Continuation (72) Inventor Akira Hirano 3-2-1, Saiwaicho, Hitachi-shi, Ibaraki Hitachi Engineering Co., Ltd.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】大気を吸込み圧縮する圧縮機と、圧縮され
た空気に燃料を混合させ燃焼ガスを作る燃焼器と、前記
燃焼ガスにより動力を発生するタービンと、前記タービ
ンの出口の排気ガスにより蒸気を発生させる排熱回収ボ
イラとを備えたガスタービン設備において、前記圧縮機
と前記燃焼器の間に再生器を設け、前記圧縮機の出口空
気を排熱回収ボイラで発生した蒸気で加熱することを特
徴とする蒸気利用再生サイクルガスタービン設備。
1. A compressor for sucking and compressing the atmosphere, a combustor for mixing compressed air with fuel to produce combustion gas, a turbine for generating power by the combustion gas, and exhaust gas at the outlet of the turbine. In a gas turbine facility including an exhaust heat recovery boiler that generates steam, a regenerator is provided between the compressor and the combustor, and the outlet air of the compressor is heated by the steam generated in the exhaust heat recovery boiler. A steam-utilized regenerative cycle gas turbine facility characterized by the following.
【請求項2】請求項1において、前記圧縮機の抽出空気
と前記排熱回収ボイラの給水とを熱交換させる熱交換器
を設けた蒸気利用再生サイクルガスタービン設備。
2. The steam-utilizing regeneration cycle gas turbine facility according to claim 1, further comprising a heat exchanger for exchanging heat between the extracted air of the compressor and the feed water of the exhaust heat recovery boiler.
JP14329393A 1993-06-15 1993-06-15 Regeneration cycle gas turbine equipment using steam Pending JPH074263A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP14329393A JPH074263A (en) 1993-06-15 1993-06-15 Regeneration cycle gas turbine equipment using steam

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP14329393A JPH074263A (en) 1993-06-15 1993-06-15 Regeneration cycle gas turbine equipment using steam

Publications (1)

Publication Number Publication Date
JPH074263A true JPH074263A (en) 1995-01-10

Family

ID=15335368

Family Applications (1)

Application Number Title Priority Date Filing Date
JP14329393A Pending JPH074263A (en) 1993-06-15 1993-06-15 Regeneration cycle gas turbine equipment using steam

Country Status (1)

Country Link
JP (1) JPH074263A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2014159525A1 (en) * 2013-03-14 2014-10-02 Dresser-Rand Company Caes plant using steam injection and bottoming cycle expander

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2014159525A1 (en) * 2013-03-14 2014-10-02 Dresser-Rand Company Caes plant using steam injection and bottoming cycle expander

Similar Documents

Publication Publication Date Title
US5495709A (en) Air reservoir turbine
US4951460A (en) Apparatus and method for optimizing the air inlet temperature of gas turbines
EP1860300B1 (en) High humidity gas turbine equipment
JPS6211166B2 (en)
JPH08510311A (en) High efficiency multi-axis reheat turbine using intercooling and recuperation
JPH0826780B2 (en) Partially regenerative two-fluid gas turbine
JPH10184315A (en) Gas turbine generator
JP5909429B2 (en) Moisture gas turbine system
JP2001115859A (en) CAES power generation system
JP2003161164A (en) Combined cycle power plant
JP3961653B2 (en) Power plant
US5435123A (en) Environmentally acceptable electric energy generation process and plant
CN100470168C (en) Combined heat and power system
JPH074263A (en) Regeneration cycle gas turbine equipment using steam
JPS63201488A (en) Sintering exhaust-heat recovery device
CN114963281B (en) Combined heat and power generation system with energy storage system and coal-fired unit coupled and operation method
JPH09203327A (en) Gas turbine generator
CN116857847A (en) A combined refrigeration system utilizing gas turbine waste heat
JP2003021301A (en) Boiler facility, combined cycle gas turbine generating system, combined cycle plant, and water recovering method for facility plant
JPH10325336A (en) Gas turbine power generating system
CN217004421U (en) MDF board production system comprehensively utilizing exhaust gas of thermal power plant
JP2869070B2 (en) Gas turbine unit for electricity and heat generation and method of operation thereof
JP2000291445A (en) Gas turbine plant and operation method thereof
CN219867910U (en) Waste heat recycling system of household garbage incineration power plant
CN218760133U (en) Gas and steam combined cycle generator set flexible operation system for energy storage