JPH0979046A - Blast furnace gas combustion gas turbine - Google Patents

Blast furnace gas combustion gas turbine

Info

Publication number
JPH0979046A
JPH0979046A JP23384595A JP23384595A JPH0979046A JP H0979046 A JPH0979046 A JP H0979046A JP 23384595 A JP23384595 A JP 23384595A JP 23384595 A JP23384595 A JP 23384595A JP H0979046 A JPH0979046 A JP H0979046A
Authority
JP
Japan
Prior art keywords
gas
blast furnace
fuel gas
fuel
dust collector
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.)
Withdrawn
Application number
JP23384595A
Other languages
Japanese (ja)
Inventor
Yasuhiro Hashimoto
安弘 橋本
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 JP23384595A priority Critical patent/JPH0979046A/en
Publication of JPH0979046A publication Critical patent/JPH0979046A/en
Withdrawn legal-status Critical Current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

PROBLEM TO BE SOLVED: To eliminate dispersion of a fuel calorie caused by a difference in calorie in between a return pipe from a fuel gas compressor outlet and a main pipe, while removing a bad influence of dust in gas relating to an axial flow fuel gas compressor, in a gas turbine with blast furnace gas serving as the fuel. SOLUTION: A dust collector 5 is provided in an inlet of a fuel gas compressor 6, also a return destination of a return pipe 14 serves as an inlet of this dust collector 5. Gas advanced into the fuel gas compressor 6 is sufficiently dust arrested by the dust collector 5, gas in a main pipe and gas joining from the return pipe 14 are sufficiently mixed by this dust collector 5, and dispersion of a calorie is eliminated.

Description

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

【0001】[0001]

【発明の属する技術分野】本発明は、高炉ガス焚ガスタ
ービンの燃料ガス圧縮機の燃料ガス戻りラインとその戻
りラインの戻し位置に関する。
TECHNICAL FIELD The present invention relates to a fuel gas return line of a fuel gas compressor of a blast furnace gas fired gas turbine and a return position of the return line.

【0002】[0002]

【従来の技術】高炉ガスは鉄鉱石を溶解して銑鉄を生成
する際に発生する副生的なガスであり、可燃性成分を含
んでいるのでガスタービンの燃料ガスとして使われてい
る。
2. Description of the Related Art Blast furnace gas is a by-product gas generated when iron ore is melted to produce pig iron. Since it contains a combustible component, it is used as a fuel gas for a gas turbine.

【0003】高炉ガス中には、FeO、Fe2 2 など
の酸化鉄の粉塵や腐食ガス成分などが含まれている。ま
た高炉ガス焚ガスタービンの燃料は、転炉などから副生
する2種類以上の燃料を混合して、ガスタービンの燃焼
に必要なカロリーまで増燃している。しかし増燃ガスは
非常に微圧であるため、燃料ガス圧縮機で高圧に圧縮し
ガスタービン燃焼器に送っている。
The blast furnace gas contains iron oxide dust such as FeO and Fe 2 O 2 and corrosive gas components. The fuel for the blast furnace gas-fired gas turbine is a mixture of two or more types of fuel that are by-produced from a converter or the like, and is burned up to the calorie required for combustion in the gas turbine. However, since the accelerating gas has a very low pressure, it is compressed to a high pressure by the fuel gas compressor and sent to the gas turbine combustor.

【0004】図2は従来の高炉ガス焚ガスタービンの一
例を示す系統図である。高炉(1)で発生した高炉ガス
は、集塵装置(2)で集塵されて高炉ガスホルダー
(3)に貯められる。そして使用する際には、高炉ガス
ホルダー(3)から取り出され、混合器(4)内で別の
燃料ガスと混合された後、燃料ガス圧縮機(6)に吸気
・圧縮される。そして燃焼器(9)に送られ、ガスター
ビン(7)の空気圧縮機(8)による圧縮空気と混合し
燃焼してガスタービン(7)を駆動する。
FIG. 2 is a system diagram showing an example of a conventional blast furnace gas-fired gas turbine. The blast furnace gas generated in the blast furnace (1) is collected by the dust collector (2) and stored in the blast furnace gas holder (3). When it is used, it is taken out of the blast furnace gas holder (3), mixed with another fuel gas in the mixer (4), and then sucked and compressed by the fuel gas compressor (6). Then, it is sent to the combustor (9) and mixed with the compressed air by the air compressor (8) of the gas turbine (7) and burned to drive the gas turbine (7).

【0005】また燃料ガス圧縮機(6)は、部分負荷運
転で燃料ガスが少量ですむ時でも、サージングを避ける
ため、ある限度以下には吐出量を下げず、余った燃料ガ
スはガス戻りライン(14)によって混合器(4)の出
口部に戻している。なお符号(15)は再循環制御弁、
符号(16)は燃料ガス冷却器である。
Further, the fuel gas compressor (6) does not reduce the discharge amount below a certain limit in order to avoid surging even when a small amount of fuel gas is required in the partial load operation, and the surplus fuel gas is returned to the gas return line. It is returned to the outlet of the mixer (4) by (14). Reference numeral (15) is a recirculation control valve,
Reference numeral (16) is a fuel gas cooler.

【0006】[0006]

【発明が解決しようとする課題】前記従来の高炉ガス焚
ガスタービンには次のような解決すべき課題があった。
The conventional blast furnace gas-fired gas turbine has the following problems to be solved.

【0007】1)前述したように酸化鉄の粉塵が含まれ
ているので、高炉ガスには高炉の出口で集塵している
が、微粉末にいたるまで完全に取り除くことは不可能で
ある。したがって集塵装置を通過した粉塵が燃料ガス圧
縮機(軸流式)に吸込まれ、翼面に打痕を残したり、翼
面に付着して性能や寿命を少なからぬ影響を与えるなど
している。
1) As described above, since iron oxide dust is contained, the blast furnace gas collects dust at the outlet of the blast furnace, but it is impossible to completely remove even fine powder. Therefore, the dust that has passed through the dust collector is sucked into the fuel gas compressor (axial flow type), leaving dent marks on the blade surface and adhering to the blade surface, which considerably affects performance and life. .

【0008】2)また燃料ガス圧縮機は、軸流式である
のでサージング領域が広く、50〜60%以上の流量で
運転しないとサージングを起す。したがって低負荷運転
で燃料ガスが少量でよい場合は、サージングを生じない
範囲で運転し、余剰分は吸気側母管に戻さなければなら
ないが、配管や燃料ガス冷却器等の中を燃料ガスが流れ
る間にガスの濃淡が生じて、母管と戻り管のカロリーが
相違してくるため、その合流点よりも下流では燃料カロ
リーにバラツキが生じ、ガスタービンの回転数や負荷が
変動する。
2) Further, since the fuel gas compressor is of the axial flow type, it has a wide surging region and causes surging unless it is operated at a flow rate of 50 to 60% or more. Therefore, in the case of low load operation and a small amount of fuel gas, it is necessary to operate in a range that does not cause surging and return the surplus to the intake side mother pipe, but the fuel gas does not flow through the piping and fuel gas cooler. The light and shade of the gas occur during the flow, and the calories of the mother pipe and the return pipe become different, so that the fuel calorie varies downstream of the confluence, and the rotational speed and load of the gas turbine fluctuate.

【0009】[0009]

【課題を解決するための手段】本発明者は、前記従来の
課題を解決するために、高炉から排出された高炉ガスを
燃料ガス圧縮機で加圧した後、燃焼器で燃焼させる高炉
ガス焚ガスタービンにおいて、上記燃料ガス圧縮機の入
口に設けられた集塵器と、上記燃料ガス圧縮機の出口か
ら分岐して上記集塵器の入口に連通する燃料ガス戻りラ
インと、同燃料ガス戻りラインに設けられた燃料ガス再
循環制御弁および燃料ガス冷却器とを備えたことを特徴
とする高炉ガス焚ガスタービンを提案するものである。
In order to solve the above-mentioned conventional problems, the present inventor pressurizes a blast furnace gas discharged from a blast furnace with a fuel gas compressor and then burns it in a combustor. In the gas turbine, a dust collector provided at the inlet of the fuel gas compressor, a fuel gas return line that branches from the outlet of the fuel gas compressor and communicates with the inlet of the dust collector, and the fuel gas return line A blast furnace gas-fired gas turbine characterized by comprising a fuel gas recirculation control valve and a fuel gas cooler provided in a line.

【0010】上記のとおり本発明では、燃料ガス圧縮機
の入口に集塵器を設けたので、高炉出口の集塵装置を通
過した微粉塵末は更に捕集され、燃料ガス圧縮機に吸込
まれる粉塵は僅少となる。したがって粉塵による翼面へ
の打痕、付着も僅少となり、性能低下も抑制されて、寿
命も延びる。
As described above, in the present invention, since the dust collector is provided at the inlet of the fuel gas compressor, the fine dust powder that has passed through the dust collector at the blast furnace outlet is further collected and sucked into the fuel gas compressor. The amount of dust that is generated is very small. Therefore, dents and adhesion to the blade surface due to dust are minimal, deterioration of performance is suppressed, and life is extended.

【0011】また、燃料ガス圧縮機の出口から分岐した
燃料ガス戻りラインを集塵器入口に連通させたので、容
積の大きい集塵器内で元ガスと戻りガスとは充分に混合
され、カロリーは均一化される。したがって母管と戻り
管のカロリーの差異によって起る燃料カロリーのバラツ
キも解消され、それに起因するガスタービンの回転数や
負荷の変動もなくなって、高炉ガス焚ガスタービンプラ
ントの信頼性が向上する。
Further, since the fuel gas return line branched from the outlet of the fuel gas compressor is communicated with the dust collector inlet, the source gas and the return gas are sufficiently mixed in the dust collector having a large volume, and the calorie is reduced. Are homogenized. Therefore, the variation in the fuel calorie caused by the difference in the calorie between the mother pipe and the return pipe is also eliminated, and the fluctuation in the rotational speed and the load of the gas turbine due to it is eliminated, and the reliability of the blast furnace gas-fired gas turbine plant is improved.

【0012】[0012]

【発明の実施の形態】図1は本発明の実施の一形態に係
る高炉ガス焚ガスタービンを示す系統図である。高炉
(1)から発生した高炉ガスは、集塵装置(2)に入
り、ガス中の酸化鉄粉や粉塵などを除去され高炉ガスホ
ルダー(3)に貯えられる。使用時に高炉ガスホルダー
(3)から取り出された高炉ガスは、混合器(4)で転
炉その他で発生する副生ガスと混合されてガスタービン
燃焼に必要なカロリーまで増燃され、集塵器(5)に入
り、燃料ガス圧縮機(6)に影響を与えない程度まで粉
塵を取り除かれた後、燃料ガス圧縮機(6)に吸込まれ
る。そしてこの燃料ガス圧縮機(6)によって圧縮され
た燃料ガスは、ガスタービン(7)の空気圧縮機(8)
を出た圧縮空気と燃焼器(9)内で混合され燃焼して、
ガスタービン(7)を駆動し排気ガスとなって、更に廃
ガスボイラ(10)で蒸気を生成し、蒸気タービン(1
1)の動力源となる。なお符号(12)は発電機、符号
(13)は復水器をそれぞれ示す。
FIG. 1 is a system diagram showing a blast furnace gas-fired gas turbine according to an embodiment of the present invention. The blast furnace gas generated from the blast furnace (1) enters the dust collector (2), iron oxide powder, dust, etc. in the gas are removed and stored in the blast furnace gas holder (3). The blast furnace gas taken out from the blast furnace gas holder (3) at the time of use is mixed with the by-product gas generated in the converter or the like in the mixer (4) to increase the calorie required for gas turbine combustion, and the dust collector. (5), the dust is removed to the extent that it does not affect the fuel gas compressor (6), and then the fuel gas compressor (6) is sucked. Then, the fuel gas compressed by the fuel gas compressor (6) is supplied to the air compressor (8) of the gas turbine (7).
The mixed compressed air and the combustor (9) are burned.
The gas turbine (7) is driven to become exhaust gas, and steam is further generated in the waste gas boiler (10), and the steam turbine (1
It becomes the power source of 1). Reference numeral (12) indicates a generator, and reference numeral (13) indicates a condenser.

【0013】ここで燃料ガス圧縮機(6)は軸流式であ
りサージング域が広い。したがって低負荷運転で燃料ガ
スが少量ですむ場合は、サージングを生じない範囲で運
転し、余剰燃料ガスを再び燃料ガス圧縮機(6)の吸込
側に戻す必要がある。符号(14)がその戻りラインで
あって、この管路には燃料ガス再循環制御弁(15)と
燃料ガス冷却器(16)が設けられ、集塵器(5)の入
口側直前に連通している。集塵器(5)の容積は、戻り
管(14)と吸込母管の容積に対し充分償える容量とし
てあるので、集塵器(5)内でガスは混合され、カロリ
ーが均一化する。
The fuel gas compressor (6) is of an axial flow type and has a wide surging range. Therefore, when a small amount of fuel gas is required in low load operation, it is necessary to operate in a range where surging does not occur and to return surplus fuel gas to the suction side of the fuel gas compressor (6) again. Reference numeral (14) is its return line, and this line is provided with a fuel gas recirculation control valve (15) and a fuel gas cooler (16) and communicates with the dust collector (5) immediately before the inlet side. are doing. Since the volume of the dust collector (5) is sufficient to compensate for the volumes of the return pipe (14) and the suction mother pipe, the gas is mixed in the dust collector (5) and the calories are made uniform.

【0014】[0014]

【発明の効果】本発明によれば、燃料ガス圧縮機に吸入
される粉塵量が僅少となるので、それによる性能低下が
抑制され、寿命も延びる。また高炉ガス焚ガスタービン
の燃料ガス圧縮機の出口から分岐して吸込側に戻る戻り
ラインと吸込母管とのカロリーのバラツキがなくなるの
で、ガスタービンの回転数や負荷の変動が生じなくな
る。したがって高炉ガス焚ガスタービンプラントの信頼
性が向上する。
According to the present invention, since the amount of dust sucked into the fuel gas compressor is very small, the deterioration in performance due to the dust is suppressed and the life is extended. Further, since there is no calorie variation between the return line branching from the outlet of the fuel gas compressor of the blast furnace gas-fired gas turbine and returning to the suction side and the suction mother pipe, fluctuations in the rotational speed and load of the gas turbine do not occur. Therefore, the reliability of the blast furnace gas-fired gas turbine plant is improved.

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

【図1】図1は本発明の実施の一形態に係る高炉ガス焚
ガスタービンを示す系統図である。
FIG. 1 is a system diagram showing a blast furnace gas-fired gas turbine according to an embodiment of the present invention.

【図2】図2は従来の高炉ガス焚ガスタービンの一例を
示す系統図である。
FIG. 2 is a system diagram showing an example of a conventional blast furnace gas-fired gas turbine.

【符号の説明】[Explanation of symbols]

(1) 高炉 (2) 集塵装置 (3) 高炉ガスホルダー (4) 混合器 (5) 集塵器 (6) 燃料ガス圧縮機 (7) ガスタービン (8) 空気圧縮機 (9) 燃焼器 (10) 廃ガスボイラ (11) 蒸気タービン (12) 発電機 (13) 復水器 (14) 燃料ガス戻りライン (15) 再循環制御弁 (16) 燃料ガス冷却器 (1) Blast furnace (2) Dust collector (3) Blast furnace gas holder (4) Mixer (5) Dust collector (6) Fuel gas compressor (7) Gas turbine (8) Air compressor (9) Combustor (10) Waste gas boiler (11) Steam turbine (12) Generator (13) Condenser (14) Fuel gas return line (15) Recirculation control valve (16) Fuel gas cooler

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 高炉から排出された高炉ガスを燃料ガス
圧縮機で加圧した後、燃焼器で燃焼させる高炉ガス焚ガ
スタービンにおいて、上記燃料ガス圧縮機の入口に設け
られた集塵器と、上記燃料ガス圧縮機の出口から分岐し
て上記集塵器の入口に連通する燃料ガス戻りラインと、
同燃料ガス戻りラインに設けられた燃料ガス再循環制御
弁および燃料ガス冷却器とを備えたことを特徴とする高
炉ガス焚ガスタービン。
1. A blast furnace gas-fired gas turbine in which a blast furnace gas discharged from a blast furnace is pressurized by a fuel gas compressor and then burned by a combustor, and a dust collector provided at an inlet of the fuel gas compressor. A fuel gas return line that branches from the outlet of the fuel gas compressor and communicates with the inlet of the dust collector,
A blast furnace gas-fired gas turbine comprising a fuel gas recirculation control valve and a fuel gas cooler provided in the fuel gas return line.
JP23384595A 1995-09-12 1995-09-12 Blast furnace gas combustion gas turbine Withdrawn JPH0979046A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP23384595A JPH0979046A (en) 1995-09-12 1995-09-12 Blast furnace gas combustion gas turbine

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP23384595A JPH0979046A (en) 1995-09-12 1995-09-12 Blast furnace gas combustion gas turbine

Publications (1)

Publication Number Publication Date
JPH0979046A true JPH0979046A (en) 1997-03-25

Family

ID=16961476

Family Applications (1)

Application Number Title Priority Date Filing Date
JP23384595A Withdrawn JPH0979046A (en) 1995-09-12 1995-09-12 Blast furnace gas combustion gas turbine

Country Status (1)

Country Link
JP (1) JPH0979046A (en)

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008157226A (en) * 2006-12-19 2008-07-10 General Electric Co <Ge> Method and system for using low btu fuel gas in gas turbine
WO2009005146A1 (en) 2007-07-04 2009-01-08 Mitsubishi Heavy Industries, Ltd. Blast furnace gas burning facility and its operation method
CN101936197A (en) * 2010-08-27 2011-01-05 宋阳 Method for reclaiming hot gas by using factory closed chimney for power generation
US20120137693A1 (en) * 2010-12-03 2012-06-07 Mitsubishi Heavy Industries, Ltd. Power plant
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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008157226A (en) * 2006-12-19 2008-07-10 General Electric Co <Ge> Method and system for using low btu fuel gas in gas turbine
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WO2009005146A1 (en) 2007-07-04 2009-01-08 Mitsubishi Heavy Industries, Ltd. Blast furnace gas burning facility and its operation method
JP2009013874A (en) * 2007-07-04 2009-01-22 Mitsubishi Heavy Ind Ltd Blast furnace gas firing facility and its operating method
EP2163749A1 (en) * 2007-07-04 2010-03-17 Mitsubishi Heavy Industries, Ltd. Blast furnace gas burning facility and its operation method
US8128862B2 (en) 2007-07-04 2012-03-06 Mitsubishi Heavy Industries, Ltd. Blast furnace gas burning facility and method for operating the same
EP2163749A4 (en) * 2007-07-04 2015-04-15 Mitsubishi Heavy Ind Ltd Blast furnace gas burning facility and its operation method
CN101936197A (en) * 2010-08-27 2011-01-05 宋阳 Method for reclaiming hot gas by using factory closed chimney for power generation
US20120137693A1 (en) * 2010-12-03 2012-06-07 Mitsubishi Heavy Industries, Ltd. Power plant
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