JPS60147539A - Gas-turbine power plant utilizing blast-furnace gas as fuel - Google Patents

Gas-turbine power plant utilizing blast-furnace gas as fuel

Info

Publication number
JPS60147539A
JPS60147539A JP188984A JP188984A JPS60147539A JP S60147539 A JPS60147539 A JP S60147539A JP 188984 A JP188984 A JP 188984A JP 188984 A JP188984 A JP 188984A JP S60147539 A JPS60147539 A JP S60147539A
Authority
JP
Japan
Prior art keywords
gas
blast furnace
furnace gas
conduit
carbon dioxide
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.)
Granted
Application number
JP188984A
Other languages
Japanese (ja)
Other versions
JPH0467567B2 (en
Inventor
Sadahiko Maeda
前田 禎彦
Tsutomu Nishide
勉 西出
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.)
Ube Corp
Original Assignee
Ube 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 Ube Industries Ltd filed Critical Ube Industries Ltd
Priority to JP188984A priority Critical patent/JPS60147539A/en
Publication of JPS60147539A publication Critical patent/JPS60147539A/en
Publication of JPH0467567B2 publication Critical patent/JPH0467567B2/ja
Granted legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02CGAS-TURBINE PLANTS; AIR INTAKES FOR JET-PROPULSION PLANTS; CONTROLLING FUEL SUPPLY IN AIR-BREATHING JET-PROPULSION PLANTS
    • F02C3/00Gas-turbine plants characterised by the use of combustion products as the working fluid
    • F02C3/20Gas-turbine plants characterised by the use of combustion products as the working fluid using a special fuel, oxidant, or dilution fluid to generate the combustion products
    • F02C3/22Gas-turbine plants characterised by the use of combustion products as the working fluid using a special fuel, oxidant, or dilution fluid to generate the combustion products the fuel or oxidant being gaseous at standard temperature and pressure
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01KSTEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
    • F01K23/00Plants characterised by more than one engine delivering power external to the plant, the engines being driven by different fluids
    • F01K23/02Plants characterised by more than one engine delivering power external to the plant, the engines being driven by different fluids the engine cycles being thermally coupled
    • F01K23/06Plants characterised by more than one engine delivering power external to the plant, the engines being driven by different fluids the engine cycles being thermally coupled combustion heat from one cycle heating the fluid in another cycle
    • F01K23/10Plants characterised by more than one engine delivering power external to the plant, the engines being driven by different fluids the engine cycles being thermally coupled combustion heat from one cycle heating the fluid in another cycle with exhaust fluid of one cycle heating the fluid in another cycle
    • F01K23/106Plants characterised by more than one engine delivering power external to the plant, the engines being driven by different fluids the engine cycles being thermally coupled combustion heat from one cycle heating the fluid in another cycle with exhaust fluid of one cycle heating the fluid in another cycle with water evaporated or preheated at different pressures in exhaust boiler

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Engine Equipment That Uses Special Cycles (AREA)

Abstract

PURPOSE:To enable to obtain a required amount of electric power with a low running cost, by increasing the calorific value of blast-furnace gas by removing CO2 gas from the blast-furnace gas, and utilizing the calorie-increased blast-furnace gas as fuel for driving a gas turbine. CONSTITUTION:Blast-furnace gas 7 is carried into a compressor 4 from a conduit 8 for raising the pressure of the blast-furnace gas 7 by the compressor 4. Then, a part of the blast-furnace gas 7 is carried into a CO2 gas absorbing tank 5 via a conduit 9 while the remaining part of the gas 7 is supplied to a gas turbine 1 via a conduit 10. In the tank 5, only CO2 gas is removed from the gas 7, and CO2 gas 12 is recovered from a conduit 11. On the other hand, the compressed blast-furnace gas, the calorific value of which is increased by removal of CO2 gas, is introduced into the gas turbine 1 via a conduit 13. Air 14 is introduced into an air compressor 3 via a conduit 15 for compressing air 14 by the air compressor 3, and then the compressed air is supplied to the gas turbine 1 via a conduit 16. Further, exhaust gas of the gas turbine 1 is introduced into a waste-heat recovering boiler 6 via a conduit 18a while low-pressure steam is introduced into said tank 5 via a generator pipe 6b and a conduit 22.

Description

【発明の詳細な説明】 〔発明の技術分野〕 この発明は高炉ガスを燃料とするガスタービン発電装置
に関し、さらに詳細にはその高炉ガスの全部、または一
部から炭酸ガスを除去して高カロリー化した高炉ガスを
燃料として用いるガスタービン発電装置に係るものであ
る。
[Detailed Description of the Invention] [Technical Field of the Invention] The present invention relates to a gas turbine power generation device that uses blast furnace gas as fuel, and more specifically, to remove carbon dioxide gas from all or part of the blast furnace gas to generate a high-calorie This relates to a gas turbine power generation device that uses converted blast furnace gas as fuel.

〔従来技術〕[Prior art]

従来から低カロリーガス、%に高炉ガス、いわゆるBF
Gをガスタービンの燃料として使用するのには、これが
低カロリーガス(例えばLHV= 670xi/Ni)
であって単独では安定した燃焼が得られないために、軽
油とかプロパンガスなどの高カロリーガス燃料による助
燃を必要とするものであった。
Conventionally, low calorie gas, mainly blast furnace gas, so-called BF
In order to use G as fuel for a gas turbine, this is a low-calorie gas (for example, LHV = 670xi/Ni).
However, since stable combustion cannot be obtained by using it alone, auxiliary combustion with high-calorie gas fuel such as light oil or propane gas is required.

〔発明の概要〕[Summary of the invention]

この発明は従来のこのような実状に鑑み、高炉ガスの全
部、または一部から炭酸ガスを除去して高カロリー化(
例えばLHV= 840KaJ/NJ ) L、、この
高カロリー化した高炉カスをガスタービン駆動用燃料と
して用い、安定した燃焼の下にガスタービンの駆動、ひ
いてはこのガスターピント同軸の発電機を駆動させて所
期の発電作用、すなわち電力を得られるようにしたもの
である。
In view of this conventional situation, this invention removes carbon dioxide gas from all or part of blast furnace gas to make it high in calories (
For example, LHV = 840KaJ/NJ) This high-calorie blast furnace scum is used as fuel for driving a gas turbine, and with stable combustion, it is used to drive the gas turbine and, in turn, to drive the gas turbine coaxial generator. It is designed to generate electricity, that is, to obtain electric power.

〔実施例〕〔Example〕

以下この発明の一丈飾物につき、添付図面を参照して詳
細に説明する。
Hereinafter, the one-length ornament of the present invention will be explained in detail with reference to the accompanying drawings.

添付図面はこの実施例装置の概要を示すブロック構成図
である。この図面において、ガスタービン1には、発電
機2と、空気圧縮機3と、高炉ガス圧縮@4とがそれぞ
れに同軸結合されてお一部、また別に炭酸ガス吸収槽5
と、廃熱回収ボイラ6とがそれぞれに設けられている。
The accompanying drawing is a block diagram showing an outline of the apparatus of this embodiment. In this drawing, a gas turbine 1 includes a generator 2, an air compressor 3, and a blast furnace gas compressor @4, each of which is coaxially coupled to a part of the gas turbine 1, and a carbon dioxide absorption tank 5 separately.
and a waste heat recovery boiler 6 are provided respectively.

しかして溶鉱炉から排出される低カロリーの高炉ガス(
BFG ) 7は、管路8から前記高炉ガス圧縮機4に
導入されて昇圧され、この昇圧圧縮された高炉ガスはそ
の一部が管路9により前記炭酸ガス吸収槽5に、他部が
管路10にょシ前記ガスタービン1にそれぞれに導入さ
れ、炭酸ガス吸収槽5では後述する熱源の下にそのガス
成分中から炭酸ガス成分のみが吸収除去されて、管路1
1がら所定の炭酸ガス12を回収すると共に、この成分
中からの炭酸ガスの除去により高カロリー化された圧縮
高炉ガスもまた管路13から前記ガスタービン1に導入
され、かつ前記管路9を経た炭酸ガス未除去の圧縮高炉
ガスと一諸にされてガスタービン駆動用の燃料となり、
また空気14は管路15から前記空気圧縮機3に導入さ
れて圧縮を受け、シ この圧縮空気ついてもまた同様に管路16から前記ガス
タービン1に導入されてガスタービン駆動用の燃焼用空
気となる。そしてこれらのそれぞれに圧縮された燃料お
よび空気の燃焼によシ駆動されるガスタービン1は、前
記各圧縮機3.4を回転駆動させて、前述したとおりに
それぞれ高炉ガスならびに空気の圧縮作用を得ると共に
、併せて前記発電機2を回転駆動させて所定の電力17
を発電させ、続いてその排ガスは管路18aから前記廃
熱回収ボイラ6に導入され、この廃熱回収ボイラ6では
それぞれに管路19を経てボイラ水1Bが供給されてい
るところの、高圧蒸気発生管6aと低圧蒸気発生管6b
とによシその廃熱が回収され、高圧蒸気発生管6aから
は管路20により所定の高圧蒸気21を取り出し、また
低圧蒸気発生管6bで発生させた低圧蒸気は、管路22
により前記炭酸ガス吸収’PI”+ 5に尋人させて、
その炭酸ガス吸収のための熱源として使用するのである
However, the low-calorie blast furnace gas discharged from the blast furnace (
The BFG) 7 is introduced into the blast furnace gas compressor 4 through a pipe 8 and is pressurized, and part of this pressurized and compressed blast furnace gas is sent to the carbon dioxide absorption tank 5 via a pipe 9, and the other part is sent to the pipe 9. The pipes 10 are respectively introduced into the gas turbine 1, and in the carbon dioxide absorption tank 5, only the carbon dioxide component is absorbed and removed from the gas components under a heat source to be described later.
A predetermined amount of carbon dioxide gas 12 is recovered from the gas turbine 1, and the compressed blast furnace gas, which has been made high in calories by removing the carbon dioxide gas from this component, is also introduced into the gas turbine 1 through the pipe line 13, and through the pipe line 9. It is combined with the compressed blast furnace gas that has undergone carbon dioxide removal and becomes the fuel for driving the gas turbine.
Air 14 is introduced into the air compressor 3 through a pipe 15 and is compressed, and the compressed air is also introduced into the gas turbine 1 through a pipe 16 to become combustion air for driving the gas turbine. becomes. The gas turbine 1, which is driven by the combustion of the fuel and air compressed in each of these, drives each of the compressors 3.4 to rotate, and compresses the blast furnace gas and air, respectively, as described above. At the same time, the generator 2 is rotationally driven to generate a predetermined electric power 17.
The exhaust gas is then introduced into the waste heat recovery boiler 6 through the pipe 18a, and in the waste heat recovery boiler 6, the high-pressure steam is supplied to each boiler water 1B via the pipe 19. Generation pipe 6a and low pressure steam generation pipe 6b
The waste heat is recovered, and a predetermined amount of high-pressure steam 21 is taken out from the high-pressure steam generation pipe 6a through the pipe 20, and the low-pressure steam generated in the low-pressure steam generation pipe 6b is taken out through the pipe 22.
According to the carbon dioxide absorption 'PI''+5,
It is used as a heat source to absorb carbon dioxide gas.

このようにしてこの実施例装置においては、高炉ガスを
燃料にして所期の電力を得ると共に、併せて炭酸ガスな
らびに高圧蒸気を得ることができるのである。こ\でこ
の実施例装置から得られる実質的な結果としては、その
装置規模によつ1も異なるが、採譜的に引き合う装置規
模での一例としてのそれを数値で表わすと次のとおりで
あった。
In this way, in this embodiment of the apparatus, the desired electric power can be obtained by using blast furnace gas as fuel, and at the same time, carbon dioxide gas and high-pressure steam can be obtained. The actual results obtained from this embodiment of the apparatus differ depending on the scale of the apparatus, but when expressed numerically as an example of the scale of the apparatus that can be used for music transcription, it is as follows. Ta.

すなわち、入力側に ・高炉ガス(BFG) 40℃ I F1a at a
88−00nNn!/HΦボイラ給水 105℃ 1.
23ata 40.6T/Hを導入するようにした場合
、出力側で ・発電機軸端での出力 16,766KW/H・高圧蒸
気量 380℃31.5庭し−G 32.8T/H・炭
酸ガス量 99.5%ω℃5に屹G 3.薗ON献/H
を得た。
That is, on the input side, blast furnace gas (BFG) 40℃ I F1a at a
88-00nNn! /HΦBoiler feed water 105℃ 1.
When introducing 23ata 40.6T/H, on the output side - Output at the end of the generator shaft 16,766KW/H - High pressure steam amount 380℃ 31.5 days - G 32.8T/H - Carbon dioxide gas Amount: 99.5%ω℃5G 3. Soon ON dedication/H
I got it.

なお、前記実施例においては、炭酸ガス圧縮機によって
得られる圧縮炭酸ガスの一部を炭酸ガス吸収槽に、他部
をそのま\ガスタービンに導入するようにしているが、
圧縮炭酸ガスの全部を炭酸ガス吸収槽に導入するように
してもよいことは勿論である。
In the above embodiment, a part of the compressed carbon dioxide obtained by the carbon dioxide compressor is introduced into the carbon dioxide absorption tank, and the other part is directly introduced into the gas turbine.
Of course, all of the compressed carbon dioxide gas may be introduced into the carbon dioxide absorption tank.

〔発明の効果〕〔Effect of the invention〕

以上詳述したように、この発明によるときは、高炉ガス
の全部または一部からその成分中の炭酸ガスを除去して
高カロリー化し、この高カロリー化高炉ガスのみを燃料
にして安定した燃焼を行なわせ、発電機を結合したガス
タービンを回転駆動させるようにしたから、従来のよう
に別の高カロリー燃料2例えば軽油とかプロパンガスな
どを助燃剤として使用する必要がなく、低摩な運転コス
トで所用の電力を得ることができ、また副産物として従
来と同様に高圧蒸気は勿論のこと、新たに純度の高い炭
酸ガスを回収することができるなどの特長を有するもの
である。
As detailed above, according to the present invention, carbon dioxide in the components is removed from all or part of blast furnace gas to make it high in calories, and stable combustion is achieved using only this high calorie blast furnace gas as fuel. Since the gas turbine connected to the generator is driven to rotate, there is no need to use another high-calorie fuel such as diesel oil or propane gas as a combustion improver, resulting in low friction and low operating costs. This system has the advantage of being able to obtain the required electricity, and as a by-product, not only high-pressure steam as in the past, but also highly purified carbon dioxide gas can be recovered.

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

図面はこの発明に係る高炉ガスを燃料とするガスタービ
ン発電装置の一実施例装置の概要を示すブロック栴成図
である。 1 ・ψIII+ガスタービン、2・・・俸発電機、3
・・・・空気圧縮機、4・・・・高炉ガス圧縮機、5・
−・・炭酸ガス吸収槽、6・拳・・廃熱回収ボイラ。 特許出願人 宇部興産株式会社 代 理 人 山川数構(はか2名)
The drawing is a block diagram schematically showing an embodiment of a gas turbine power generation device using blast furnace gas as fuel according to the present invention. 1 ・ψIII+gas turbine, 2...salary generator, 3
... Air compressor, 4... Blast furnace gas compressor, 5.
-... Carbon dioxide absorption tank, 6. Fist... Waste heat recovery boiler. Patent Applicant: Ube Industries Co., Ltd. Agent: Kazuki Yamakawa (2 people)

Claims (1)

【特許請求の範囲】[Claims] 発電機駆動用のガスタービンと、少なくともこのガスタ
ービンに同軸結合されて駆動される高炉ガス圧縮機およ
び空気圧縮機と、炭酸ガス吸収槽および廃熱回収ボイラ
とをiし、前記高炉ガス圧縮機により昇圧される圧縮高
炉ガスを炭酸ガス吸収槽に導入して、導入された高炉ガ
ス中の炭酸ガス成分を吸収除去させると共に、この炭酸
ガス成分が除去されて高カロリーガスとされた全部の圧
縮高炉ガス、またはこの一部の圧縮高炉ガスと、前記昇
圧されたま\の他部の圧縮高炉ガスとを燃料として用い
、この燃料と前記空気圧縮機からの圧縮された燃焼用空
気との燃焼ガスにより前記ガスタービンを駆動して発電
させ、さらにこのガスタービン駆動後の排ガスを前記廃
熱回収ボイラに導入して、とのボイラによシ高圧および
低圧蒸気を発生させ、かつこの低圧蒸気を前記炭酸ガス
吸収槽に熱源として導入させるように構成させたことを
特徴とする高炉ガスを燃料とするガスタービン発電装置
A gas turbine for driving a generator, at least a blast furnace gas compressor and an air compressor that are coaxially coupled to and driven by the gas turbine, a carbon dioxide absorption tank and a waste heat recovery boiler, and the blast furnace gas compressor The compressed blast furnace gas that has been pressurized is introduced into a carbon dioxide absorption tank to absorb and remove the carbon dioxide component in the introduced blast furnace gas, and the entire compressed gas from which this carbon dioxide component has been removed is converted into high-calorie gas. Blast furnace gas, or a part of the compressed blast furnace gas, and the pressurized and other part of the compressed blast furnace gas are used as fuel, and a combustion gas of this fuel and compressed combustion air from the air compressor is used. The gas turbine is driven to generate electricity, and the exhaust gas after driving the gas turbine is introduced into the waste heat recovery boiler to generate high-pressure and low-pressure steam, and the low-pressure steam is A gas turbine power generation device using blast furnace gas as fuel, characterized in that it is configured to be introduced into a carbon dioxide absorption tank as a heat source.
JP188984A 1984-01-11 1984-01-11 Gas-turbine power plant utilizing blast-furnace gas as fuel Granted JPS60147539A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP188984A JPS60147539A (en) 1984-01-11 1984-01-11 Gas-turbine power plant utilizing blast-furnace gas as fuel

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP188984A JPS60147539A (en) 1984-01-11 1984-01-11 Gas-turbine power plant utilizing blast-furnace gas as fuel

Publications (2)

Publication Number Publication Date
JPS60147539A true JPS60147539A (en) 1985-08-03
JPH0467567B2 JPH0467567B2 (en) 1992-10-28

Family

ID=11514140

Family Applications (1)

Application Number Title Priority Date Filing Date
JP188984A Granted JPS60147539A (en) 1984-01-11 1984-01-11 Gas-turbine power plant utilizing blast-furnace gas as fuel

Country Status (1)

Country Link
JP (1) JPS60147539A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2663685A1 (en) * 1990-06-20 1991-12-27 Zimmermann & Jansen Gmbh PROCESS FOR RECOVERING THE ENERGY FROM GAS FROM A BLAST FURNACE, AND INSTALLATION OF A BLAST FURNACE FOR CARRYING OUT THIS PROCESS.
JP2009221574A (en) * 2008-03-18 2009-10-01 Nippon Steel Engineering Co Ltd Method for separation-recovering carbon-dioxide from blast furnace gas
JP2009221575A (en) * 2008-03-18 2009-10-01 Nippon Steel Engineering Co Ltd Method for separation-recovering carbon-dioxide from blast furnace gas in utilizing process for blast furnace gas

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2663685A1 (en) * 1990-06-20 1991-12-27 Zimmermann & Jansen Gmbh PROCESS FOR RECOVERING THE ENERGY FROM GAS FROM A BLAST FURNACE, AND INSTALLATION OF A BLAST FURNACE FOR CARRYING OUT THIS PROCESS.
JP2009221574A (en) * 2008-03-18 2009-10-01 Nippon Steel Engineering Co Ltd Method for separation-recovering carbon-dioxide from blast furnace gas
JP2009221575A (en) * 2008-03-18 2009-10-01 Nippon Steel Engineering Co Ltd Method for separation-recovering carbon-dioxide from blast furnace gas in utilizing process for blast furnace gas

Also Published As

Publication number Publication date
JPH0467567B2 (en) 1992-10-28

Similar Documents

Publication Publication Date Title
US4785622A (en) Integrated coal gasification plant and combined cycle system with air bleed and steam injection
US4250704A (en) Combined gas-steam power plant with a fuel gasification device
US5485719A (en) Integration of combustor-turbine units and integral-gear pressure processors
US7284362B2 (en) Integrated air separation and oxygen fired power generation system
US4528811A (en) Closed-cycle gas turbine chemical processor
RU2009389C1 (en) Gas-distributing station with power plant
JP2011017341A (en) Method and system for providing power for coolant compression reduced in carbon dioxide emission amount and electrical power for light hydrocarbon gas liquefying process
EP0184137A1 (en) Integrated coal gasification plant and combined cycle system with air bleed and steam injection
JP3138474B2 (en) Low calorific value gas combustion apparatus and combustion method
US6216441B1 (en) Removal of inert gases from process gases prior to compression in a gas turbine or combined cycle power plant
US6061936A (en) Synthesis gas expander located immediately upstream of combustion turbine
RU2441988C2 (en) Compression unit
US6314715B1 (en) Modified fuel gas turbo-expander for oxygen blown gasifiers and related method
JPS60147539A (en) Gas-turbine power plant utilizing blast-furnace gas as fuel
CA2618030A1 (en) A method for operating a gas turbine and a gas turbine for implementing the method
GB1408174A (en) Power plant
KR101298543B1 (en) Apparatus and Method for Treating Waste Gas
JP3110114B2 (en) CO2 recovery power plant
JPH0814062A (en) Composite generating plant
JP2647582B2 (en) How to generate electricity while producing carbon dioxide and inert gas
JP3225940U (en) Power-saving facility type coal gasification combined cycle power generation facility
KR102113799B1 (en) System and Method for Direct-Fired Supercritical CO2 Power Generation of Sub-MWe
JPS58200013A (en) Gasification power generating device
RU2083914C1 (en) Gas supply system
JPH11200885A (en) Gasifying combined power generation equipment