JPH09112213A - Boiler facility for recovering waste heat from gas turbine - Google Patents

Boiler facility for recovering waste heat from gas turbine

Info

Publication number
JPH09112213A
JPH09112213A JP26668095A JP26668095A JPH09112213A JP H09112213 A JPH09112213 A JP H09112213A JP 26668095 A JP26668095 A JP 26668095A JP 26668095 A JP26668095 A JP 26668095A JP H09112213 A JPH09112213 A JP H09112213A
Authority
JP
Japan
Prior art keywords
gas
supply line
fuel gas
heat recovery
boiler
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
JP26668095A
Other languages
Japanese (ja)
Inventor
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 Engineering Co Ltd
Hitachi Ltd
Original Assignee
Hitachi Engineering Co Ltd
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, Hitachi Ltd filed Critical Hitachi Engineering Co Ltd
Priority to JP26668095A priority Critical patent/JPH09112213A/en
Publication of JPH09112213A publication Critical patent/JPH09112213A/en
Pending legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To provide a boiler facility for recovering waste heat from a gas turbine, in which unburnt gas discharged from a vent and a drain from a fuel gas supply line is stored in a gas holder and is then fed into a waste heat recovering boiler. SOLUTION: A boiler facility for recovering waste heat from a gas turbine 25 comprises a fuel gas supply line 30 incorporating components for purifying fuel gas fed into a gas turbine 25 and a waste heat recovering boiler 32, drain tanks 9, 14 receiving removed impurities, vent pipes 6, 16 for discharging fuel gas from drain tanks 9, 14, a nitrogen gas supply line 17 and a fuel gas vent pipe 19 incorporated in the supply line 30, and a gas holder 43 having an inlet side connected thereto with the vent pipe 19. A heat recovering boiler 32 is connected to the outlet of an exhaust gas duct 26 of the turbine 25 and an outlet pipe 42 of the gas holder 43 is connected to the fuel gas supply line 30 connected to the boiler 32.

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】本発明はガスタービンと排熱
回収ボイラ設備に関する。
TECHNICAL FIELD The present invention relates to a gas turbine and an exhaust heat recovery boiler facility.

【0002】[0002]

【従来の技術】図2は従来のガスタービン排熱回収ボイ
ラ設備の構成図である。低圧燃料ガス供給ライン1は、
ガス圧縮機2の圧縮機吸込セパレータ3の上流側で、ボ
イラ用燃料ガス供給ライン30と分岐し、排熱回収ボイ
ラ32に入る前で、ボイラ吸込セパレータ31により不
純物を除去する。一方、圧縮機吸込セパレータで不純物
を除去された天然ガスは、ガス圧縮機で昇圧され高圧燃
料ガス供給ライン5により圧縮機吐出セパレータ4に導
びかれ、ここで圧縮機より排出される不純物を除去す
る。各セパレータの底に不純物があるレベルまで溜る
と、手動又は自動的にドレンタンク9に排出される。こ
の時、不純物と一緒に天然ガスも排出するので、ベント
管6によりフレアスタック7に送られる。高圧燃料ガス
供給ラインで天然ガスは、ガスタービン25の燃焼器8
に入る前で、ノックアウトドラム10により、不純物を
除去される。この不純物は、ある程度溜ると、ドレンタ
ンク14に排出される。
2. Description of the Related Art FIG. 2 is a block diagram of a conventional gas turbine exhaust heat recovery boiler facility. The low pressure fuel gas supply line 1
On the upstream side of the compressor suction separator 3 of the gas compressor 2, before branching to the boiler fuel gas supply line 30 and entering the exhaust heat recovery boiler 32, impurities are removed by the boiler suction separator 31. On the other hand, the natural gas from which impurities have been removed by the compressor suction separator is pressurized by the gas compressor and guided to the compressor discharge separator 4 by the high-pressure fuel gas supply line 5, where impurities discharged from the compressor are removed. To do. When impurities are accumulated to a certain level at the bottom of each separator, they are discharged to the drain tank 9 manually or automatically. At this time, the natural gas is discharged together with the impurities, so that the natural gas is sent to the flare stack 7 through the vent pipe 6. Natural gas is supplied to the high pressure fuel gas supply line through the combustor 8 of the gas turbine 25.
Prior to entering, the knockout drum 10 removes impurities. When the impurities are accumulated to some extent, they are discharged to the drain tank 14.

【0003】ガスタービンに供給される燃料は、天然ガ
スの他に、液化ガスも併用され、まずベーパライザ11
で気化され燃料ガスとなり、ヒータ12で加熱して、ミ
ストセパレータ13で水分や液化ガスを除去後、燃焼器
に供給される。ミストレパレータもある程度不純物が溜
ると、ドレンタンク14に排出され、減圧される事によ
り液化ガス分は気化して、燃料ガスとなる。ノックアウ
トドラム10から不純物を排出する時に、天然ガスも同
時に出てくるので、ドレンタンク14からベント管16
でフレアスタックに送られる。
As the fuel supplied to the gas turbine, liquefied gas is also used in addition to natural gas. First, the vaporizer 11 is used.
Is vaporized into fuel gas, which is heated by the heater 12 to remove water and liquefied gas by the mist separator 13 and then supplied to the combustor. If impurities are accumulated to some extent in the mistreparator, the liquefied gas is vaporized by being discharged to the drain tank 14 and depressurized to become fuel gas. When the impurities are discharged from the knockout drum 10, natural gas also comes out at the same time, so the drain tank 14 to the vent pipe 16
And sent to the flare stack.

【0004】各機器や配管を分解して、点検や補修を行
う前は、各燃料供給ライン内に有る残留ガスを窒素ガス
に置換する必要がある。この方法は、各燃料供給ライン
の下流側に設けたベント弁15を開き、ベント管19に
より残留ガスをフレアスタックに送り、各ラインを大気
圧まで下げる。次に各ラインの上流側に設けた窒素ガス
供給ライン17の窒素ガス止弁18を開き、各ラインに
窒素ガスを出す事により、残留ガスをフレアスタックに
追い出して、窒素ガスに置換する。フレアスタックで
は、先端から可燃性ガスが少量出る時は、そのまま大気
放出して拡散させ、多量に放出する場合は先端部で燃焼
させる。
Before disassembling each device or pipe for inspection or repair, it is necessary to replace the residual gas in each fuel supply line with nitrogen gas. In this method, the vent valve 15 provided on the downstream side of each fuel supply line is opened, the residual gas is sent to the flare stack through the vent pipe 19, and each line is reduced to atmospheric pressure. Next, the nitrogen gas stop valve 18 of the nitrogen gas supply line 17 provided on the upstream side of each line is opened, and nitrogen gas is discharged to each line, thereby expelling the residual gas to the flare stack and replacing it with nitrogen gas. In the flare stack, when a small amount of combustible gas is emitted from the tip, it is emitted to the atmosphere and diffused, and when a large amount is emitted, it is burned at the tip.

【0005】未燃ガスの処理に関する方法として、特開
昭57−87529 号公報が有るが、同様にフレアスタックに
送り燃焼させる。
As a method for treating unburned gas, there is Japanese Patent Laid-Open No. 57-87529, which is similarly sent to a flare stack and burned.

【0006】[0006]

【発明が解決しようとする課題】上記従来技術では、貴
重な可燃性ガスを有効に利用しないで、フレアスタック
から大気に放出している問題がある。
The above-mentioned prior art has a problem that valuable flammable gas is not effectively utilized but is released from the flare stack to the atmosphere.

【0007】本発明の目的は、ドレン及びベントからフ
レアスタックに送り無駄に消費している未燃ガスを有効
に利用することにある。
An object of the present invention is to effectively utilize the unburned gas which is wastefully consumed by being sent from the drain and vent to the flare stack.

【0008】[0008]

【課題を解決するための手段】本発明は、フレアスタッ
クの代りにガスホルダを設け、未燃ガスを貯蔵し、ガス
ホルダ内のガス圧力は大気圧より高いので、吐出側を排
熱回収ボイラに接続すれば、エネルギを有効に利用出来
る。
According to the present invention, a gas holder is provided in place of the flare stack to store unburned gas, and the gas pressure in the gas holder is higher than atmospheric pressure. Therefore, the discharge side is connected to the exhaust heat recovery boiler. If so, the energy can be effectively used.

【0009】本発明の実施例は、排熱回収ボイラがガス
タービンの排気ガスのエネルギの他に、助燃装置を設け
蒸気をより多く発生させるもので、燃料に天燃ガスを用
いる装置である。助燃装置に送る天然ガスの一部又は全
量を、本発明のガスホルダから送れば、省エネルギ設備
となる。
The embodiment of the present invention is an apparatus in which the exhaust heat recovery boiler is provided with an auxiliary combustion device in addition to the energy of the exhaust gas of the gas turbine to generate more steam, and which uses natural gas as the fuel. If part or all of the natural gas to be sent to the auxiliary burner is sent from the gas holder of the present invention, energy saving equipment can be obtained.

【0010】[0010]

【発明の実施の形態】以下、本発明の実施例を図1,図
2により説明する。図1は、排熱回収ボイラに助燃装置
が有る実施例である。ガスホルダ40のホルダ入口管4
1には、ベント管6,ベント管16,ベント管19を接
続する。本ガスホルダに流入するガスの圧力はホルダ浮
屋根43の重量と釣合うが、ボイラ用燃料ガス供給ライ
ン30の圧力に設定する。もしガスホルダ内の圧力が高
いと、各ベント管に逆流する恐れも有るので、ホルダ入
口逆止弁44を設ける。排熱回収ボイラ32は、ガスタ
ービンの排気ダクト26と接続し、約500℃の排気ガ
ス温度で蒸気を発生させる。この発生させる蒸気量をよ
り多くしたい場合には、排熱回収ボイラに助燃装置33
を設け、ボイラ用燃料ガス供給ラインより、天然ガスを
供給する。本助燃装置は、ガスタービンが停止している
間でも、蒸気を発生出来る利点が有る。ガスホルダから
ガスを助燃装置に供給する為に、ホルダ出口管42をホ
ルダ出口逆止弁45とホルダ出口止弁46を介して、ボ
イラ用燃料ガス供給ラインに接続する。燃料ガス供給ラ
イン側のガスを半分使用する場合は、ガス供給ライン弁
34を半開し、ホルダ出口止弁46を半開する。ガスホ
ルダ側のガスで全部供給する時は、ガス供給ライン弁を
全閉し、ホルダ出口止弁を全開する。
BEST MODE FOR CARRYING OUT THE INVENTION Embodiments of the present invention will be described below with reference to FIGS. FIG. 1 shows an embodiment in which an exhaust heat recovery boiler has an auxiliary combustion device. Holder inlet pipe 4 of gas holder 40
A vent pipe 6, a vent pipe 16, and a vent pipe 19 are connected to the device 1. The pressure of the gas flowing into the gas holder balances the weight of the holder floating roof 43, but is set to the pressure of the boiler fuel gas supply line 30. If the pressure in the gas holder is high, there is a risk of backflow to each vent pipe, so a holder inlet check valve 44 is provided. The exhaust heat recovery boiler 32 is connected to the exhaust duct 26 of the gas turbine and generates steam at an exhaust gas temperature of about 500 ° C. When it is desired to increase the amount of steam generated, the auxiliary heat recovery device 33 is installed in the exhaust heat recovery boiler.
Is installed to supply natural gas from the boiler fuel gas supply line. This auxiliary combustion device has an advantage that steam can be generated even while the gas turbine is stopped. In order to supply gas from the gas holder to the auxiliary combustion apparatus, the holder outlet pipe 42 is connected to the boiler fuel gas supply line via the holder outlet check valve 45 and the holder outlet stop valve 46. When half the gas on the fuel gas supply line side is used, the gas supply line valve 34 is half-opened and the holder outlet stop valve 46 is half-opened. When supplying all of the gas on the gas holder side, fully close the gas supply line valve and fully open the holder outlet stop valve.

【0011】次に、排熱回収ボイラに助熱装置が付いて
いない一実施例を、図2により説明する。ガスホルダの
中に貯えられた天然ガスは、ホルダ出口止弁を開け、低
圧燃料ガス供給ライン止弁20を閉じて、ホルダ出口管
により低圧燃料ガス供給ラインに導かれ、圧縮機吸込セ
パレータでごみを除かれ、ガス圧縮機で加圧され、ガス
タービンに供給される。しかし、ガスホルダ内のガス
は、窒素ガスも含まれている場合も有り、これは発熱量
が不足するので、ベーパライザの液化ガスも稼働させ、
ガスタービンに燃料ガスを送る。これにより、ガスター
ビンの出力も、排熱回収ボイラでの蒸発量も低下せず運
転することができる。
Next, an embodiment in which the exhaust heat recovery boiler is not equipped with a supplementary heat device will be described with reference to FIG. The natural gas stored in the gas holder opens the holder outlet stop valve, closes the low pressure fuel gas supply line stop valve 20, is guided to the low pressure fuel gas supply line by the holder outlet pipe, and removes dust with the compressor suction separator. It is removed, pressurized with a gas compressor and fed to the gas turbine. However, the gas in the gas holder may also contain nitrogen gas, which has insufficient calorific value, so the liquefied gas of the vaporizer is also activated.
Send fuel gas to the gas turbine. As a result, the output of the gas turbine and the evaporation amount in the exhaust heat recovery boiler do not decrease, and operation can be performed.

【0012】[0012]

【発明の効果】本発明によれば、従来無駄に捨てていた
燃料を回収し、排熱回収ボイラで燃焼させ蒸気を発生さ
せる事により、エネルギを有効に活用出来る。これによ
りプラント熱効率は、消費する燃料が少なくなるので、
大幅に向上する。
According to the present invention, it is possible to effectively use energy by recovering fuel which was conventionally wasted and burned in the exhaust heat recovery boiler to generate steam. This reduces plant thermal efficiency by consuming less fuel,
Greatly improved.

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

【図1】本発明の一実施例である助燃装置付のガスター
ビン排熱回収ボイラ設備を示す系統図。
FIG. 1 is a system diagram showing a gas turbine exhaust heat recovery boiler facility with an auxiliary combustion device according to an embodiment of the present invention.

【図2】本発明の一実施例である助燃装置無のガスター
ビン排熱回収ボイラ設備を示す系統図。
FIG. 2 is a system diagram showing a gas turbine exhaust heat recovery boiler facility without an auxiliary combustion device, which is an embodiment of the present invention.

【図3】従来のガスタービン排熱回収ボイラ設備を示す
系統図。
FIG. 3 is a system diagram showing a conventional gas turbine exhaust heat recovery boiler facility.

【符号の説明】[Explanation of symbols]

6,16,19…ベント管、9,14…ドレンタンク、
25…ガスタービン、30…ボイラ用燃料ガス供給ライ
ン、32…排熱回収ボイラ、42…ホルダ出口管、43
…ガスホルダ。
6, 16, 19 ... Vent pipe, 9, 14 ... Drain tank,
25 ... Gas turbine, 30 ... Boiler fuel gas supply line, 32 ... Exhaust heat recovery boiler, 42 ... Holder outlet pipe, 43
… Gas holder.

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】ガスタービンと排熱回収ボイラに供給する
燃料ガスを、清浄にする機器を備えた燃料ガス供給ライ
ンと、除去された不純物を受入れるドレンタンクと、前
記ドレンタンク内の燃料ガスを排出するベント管を備え
た設備において、前記ベント管をガスホルダの入口管に
接続する事を特徴とするガスタービン排熱回収ボイラ設
備。
1. A fuel gas supply line equipped with a device for cleaning fuel gas supplied to a gas turbine and an exhaust heat recovery boiler, a drain tank for receiving removed impurities, and a fuel gas in the drain tank. A facility equipped with a vent pipe for discharging, wherein the vent pipe is connected to an inlet pipe of a gas holder, a gas turbine exhaust heat recovery boiler facility.
【請求項2】ガスタービンと排熱回収ボイラに供給する
燃料ガスを、清浄にする機器を備えた燃料ガス供給ライ
ンと、前記燃料ガス供給ラインに窒素ガス供給ラインと
燃料ガスベント管を備えた設備において、前記燃料ガス
ベント管をガスホルダの入口管に接続する事を特徴とす
るガスタービン排熱回収ボイラ設備。
2. A fuel gas supply line equipped with a device for cleaning the fuel gas supplied to the gas turbine and the exhaust heat recovery boiler, and a facility equipped with a nitrogen gas supply line and a fuel gas vent pipe in the fuel gas supply line. In the gas turbine exhaust heat recovery boiler facility, the fuel gas vent pipe is connected to an inlet pipe of a gas holder.
【請求項3】ガスタービンの排気ガスダクト出口に、排
熱回収ボイラを接続し、燃料ガスを前記排熱回収ボイラ
に供給する燃料ガス供給ラインを備えた設備において、
ガスホルダの出口管を前記燃料ガス供給ラインに接続す
る事を特徴とするガスタービン排熱回収ボイラ設備。
3. A facility having a fuel gas supply line for connecting an exhaust heat recovery boiler to an exhaust gas duct outlet of a gas turbine and supplying a fuel gas to the exhaust heat recovery boiler,
A gas turbine exhaust heat recovery boiler facility, wherein an outlet pipe of a gas holder is connected to the fuel gas supply line.
JP26668095A 1995-10-16 1995-10-16 Boiler facility for recovering waste heat from gas turbine Pending JPH09112213A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP26668095A JPH09112213A (en) 1995-10-16 1995-10-16 Boiler facility for recovering waste heat from gas turbine

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP26668095A JPH09112213A (en) 1995-10-16 1995-10-16 Boiler facility for recovering waste heat from gas turbine

Publications (1)

Publication Number Publication Date
JPH09112213A true JPH09112213A (en) 1997-04-28

Family

ID=17434209

Family Applications (1)

Application Number Title Priority Date Filing Date
JP26668095A Pending JPH09112213A (en) 1995-10-16 1995-10-16 Boiler facility for recovering waste heat from gas turbine

Country Status (1)

Country Link
JP (1) JPH09112213A (en)

Similar Documents

Publication Publication Date Title
US7107774B2 (en) Method and apparatus for combined cycle power plant operation
KR100406890B1 (en) Liquefied gas supply device
US8166747B2 (en) Gas turbine engine
JPH08114104A (en) Composite gas-steam turbine power plant
US20070277529A1 (en) Method and system for heat recovery from dirty gaseous fuel in gasification power plants
CZ264690A3 (en) Process for producing electric power and apparatus for making the same
FR2781252A1 (en) MIXED POWER PLANT
JP5840559B2 (en) Exhaust gas recirculation type gas turbine power plant operating method and exhaust gas recirculation type gas turbine power plant
CN1159509A (en) Operation method for equipment of electric power station
US6820432B2 (en) Method of operating a heat recovery boiler
JP2009121778A (en) Pressurized fluidized incineration facility and operation method for pressurized fluidized incineration facility
JPH09112213A (en) Boiler facility for recovering waste heat from gas turbine
JP4187894B2 (en) Flue gas denitration method
JP3952287B2 (en) Method and facility for recovering energy from combustible materials
RU2272914C1 (en) Gas-steam thermoelectric plant
JP2802504B2 (en) Coal gasifier startup or hot banking system
CN218494994U (en) Biogas combustion heating water supply system in waste incineration disposal power station
Nakajima et al. Development strategy of environmentally friendly sewage sludge incineration technologies in Bureau of Sewerage Tokyo Metropolitan Government
JPS6149490B2 (en)
JP2001303974A (en) Combined-cycle generator set
RU44145U1 (en) CONTACT STEAM-GAS POWER PLANT
JP3772029B2 (en) Gas turbine combustor fuel supply system
CN116044568A (en) Gas turbine device based on solid hydrogen fuel
SU1222860A1 (en) Steam-gas plant
JPH07119951A (en) Method for reventing white smoke in dust incinerator plant