JPS595834A - Gas turbine plant - Google Patents
Gas turbine plantInfo
- Publication number
- JPS595834A JPS595834A JP11395282A JP11395282A JPS595834A JP S595834 A JPS595834 A JP S595834A JP 11395282 A JP11395282 A JP 11395282A JP 11395282 A JP11395282 A JP 11395282A JP S595834 A JPS595834 A JP S595834A
- Authority
- JP
- Japan
- Prior art keywords
- air
- gas turbine
- temperature
- gas
- waste gas
- 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
Links
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01D—NON-POSITIVE DISPLACEMENT MACHINES OR ENGINES, e.g. STEAM TURBINES
- F01D25/00—Component parts, details, or accessories, not provided for in, or of interest apart from, other groups
- F01D25/02—De-icing means for engines having icing phenomena
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F02—COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
- F02C—GAS-TURBINE PLANTS; AIR INTAKES FOR JET-PROPULSION PLANTS; CONTROLLING FUEL SUPPLY IN AIR-BREATHING JET-PROPULSION PLANTS
- F02C7/00—Features, components parts, details or accessories, not provided for in, or of interest apart form groups F02C1/00 - F02C6/00; Air intakes for jet-propulsion plants
- F02C7/08—Heating air supply before combustion, e.g. by exhaust gases
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F02—COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
- F02C—GAS-TURBINE PLANTS; AIR INTAKES FOR JET-PROPULSION PLANTS; CONTROLLING FUEL SUPPLY IN AIR-BREATHING JET-PROPULSION PLANTS
- F02C7/00—Features, components parts, details or accessories, not provided for in, or of interest apart form groups F02C1/00 - F02C6/00; Air intakes for jet-propulsion plants
- F02C7/12—Cooling of plants
- F02C7/14—Cooling of plants of fluids in the plant, e.g. lubricant or fuel
- F02C7/141—Cooling of plants of fluids in the plant, e.g. lubricant or fuel of working fluid
- F02C7/143—Cooling of plants of fluids in the plant, e.g. lubricant or fuel of working fluid before or between the compressor stages
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
(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】
本発明は液化天然ガスなどの低温度の燃料を使用するガ
スタービン装置のガスの再気化方法に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for revaporizing gas in a gas turbine apparatus using low temperature fuel such as liquefied natural gas.
ガスタービンの最大出力および熱効率は圧縮機入口の空
気温度に影響され、この温度が高くなると最大出力およ
び熱効率は低下する。従って、大気をそのまま圧縮機に
吸込む方式の従来のガスタービン装置では、夏期等の大
気温度が高い時に最大出力が減少する問題がある。The maximum output and thermal efficiency of a gas turbine are affected by the air temperature at the compressor inlet, and as this temperature increases, the maximum output and thermal efficiency decrease. Therefore, in conventional gas turbine devices that suck atmospheric air directly into the compressor, there is a problem in that the maximum output decreases when the atmospheric temperature is high, such as in summer.
ガスタービンの燃料として使用する液化天然ガスの再気
化時の冷熱を利用し圧縮機に流入する空気温度を下げる
ことが上記の問題の一つの解決方法として考えられる。One possible solution to the above problem is to reduce the temperature of the air flowing into the compressor by utilizing the cold heat generated during revaporization of liquefied natural gas used as fuel for a gas turbine.
本発明はこの様な、圧縮機吸込空気による液化燃料の再
気化方式を有するガスタービンプラントに関するもので
再気化装置に流入する前の空気にガスタービンの廃ガス
を必要により混合させ、再気化装置に流入する加熱側の
流体(空気と廃ガスの混合気体、以下、廃ガス混合空気
と称す)の温度全制限値内に制御することであるー。The present invention relates to a gas turbine plant having a method of revaporizing liquefied fuel using compressor suction air.The present invention relates to a gas turbine plant having a method of revaporizing liquefied fuel using compressor suction air. The purpose of this is to control the temperature of the heating fluid (mixed gas of air and waste gas, hereinafter referred to as waste gas mixed air) flowing into the heating side to within the total limit value.
不発明の目的とする所は、圧縮機入口空気温度が過度に
低くなり、空気中の水分が圧縮機内で氷結し、この機器
が損傷するのを防止することである。さらに、冬期など
において大気温度が氷点下附近までに低くなると再気化
装置の気化能力が減少するので、廃ガス混合空気の温度
定められた温度以上に制限することにより々再気化装置
のTJ −を小型にすることである。The object of the invention is to prevent the compressor inlet air temperature from becoming too low, causing moisture in the air to freeze inside the compressor and damage the equipment. Furthermore, when the atmospheric temperature drops to below freezing, such as in winter, the vaporization capacity of the revaporizer decreases, so by limiting the temperature of the waste gas mixture air to a predetermined temperature or higher, the TJ - of the revaporizer can be made smaller. It is to do so.
更に、廃ガス混合空気は、酸素含有量が通常の空気より
少ないことによって、燃焼時に発生する窒素配化物を減
少する効果が得られ、環境保護ができる点にある。Furthermore, since the waste gas mixture air has a lower oxygen content than normal air, it has the effect of reducing nitrogen compounds generated during combustion, thereby protecting the environment.
以下、本発明全実施例に沿って詳細に説明する。Hereinafter, all embodiments of the present invention will be explained in detail.
第1図は本発明になるガスタービン・プラントの系統を
示す。FIG. 1 shows a system of a gas turbine plant according to the present invention.
圧縮機7に流入する空気6は、圧縮され燃焼器9に入る
。4は燃料である。燃焼ガス10は、ガスタービン11
に入り、12は廃ガスを示し、13は発電機などで負荷
である。廃ガス12は廃熱回収ボイラ14全通り16は
その廃ガスである。Air 6 entering compressor 7 is compressed and enters combustor 9 . 4 is fuel. The combustion gas 10 is passed through a gas turbine 11
12 indicates waste gas, and 13 indicates a load such as a generator. The waste gas 12 is the waste gas from the waste heat recovery boiler 14 and all the passages 16 are the waste gas.
夏期などにおいて圧縮機に流入する空気6の温度が高く
なるとガスタービンの最大出力が減少するので、これを
少くするため燃料の冷熱を利用して空気6の温度ケ低く
することが有効である。再気化装置3はこの目的のため
であり、これによって液化ガスタンク1からの低温燃料
2を流入空気51によって加熱、気化する。流入空気5
1はに2、料2の冷熱によって低温空気6となりこれが
圧縮機7に流入することになり、従ってガスタービンの
最大出力の減少を抑えることができるものである。When the temperature of the air 6 flowing into the compressor increases in summer or the like, the maximum output of the gas turbine decreases, so in order to reduce this, it is effective to lower the temperature of the air 6 using the cold heat of the fuel. The revaporizer 3 is for this purpose, whereby the cold fuel 2 from the liquefied gas tank 1 is heated and vaporized by the incoming air 51 . Incoming air 5
1 and 2, the cold heat of the feedstock 2 turns into low-temperature air 6, which flows into the compressor 7, thus making it possible to suppress a decrease in the maximum output of the gas turbine.
5は大気状態を示す。夏期など大気5の温度が高い場合
には、これ全そのまま再気化装置3に導入しても圧縮機
入口空気6の温度は極度に低下しないが、冬期など大気
5の温度が低い場合には圧縮機入口空気6の温度は氷点
下にまでなり、圧縮機7内で氷結等が起り材機を損傷す
る危険がある。5 indicates the atmospheric condition. When the temperature of the atmosphere 5 is high, such as in the summer, the temperature of the compressor inlet air 6 will not drop significantly even if the air is introduced directly into the revaporizer 3, but when the temperature of the atmosphere 5 is low, such as in the winter, the compressor The temperature of the machine inlet air 6 reaches below freezing, and there is a danger that icing will occur inside the compressor 7 and damage the lumber machine.
また、再気化装置3においても低温度の大気をそのまま
加熱流体として用いると、再気化能力が低下するので、
大型化する必要が生じたり、あるいは再気化装置内での
氷結の問題が起る。Furthermore, in the revaporization device 3, if low-temperature air is directly used as the heating fluid, the revaporization ability will decrease.
It may be necessary to increase the size of the device, or there may be a problem of freezing within the revaporizer.
すなわち、大気温度は最低氷点下から最大30r程度ま
で変動するが、これは燃料ガスの再気化装置の運転状態
を大きく変動させ、特に大気温度が低い場合においては
圧縮機等の保護等が必要となることが分る。ところで、
冬期の如く大気温度が低い場合においてはタービンの最
大出力は増大するから、夏期の如き最大出力が減少し、
負荷に対する能力が不足するという問題は起らない。In other words, the atmospheric temperature fluctuates from the lowest freezing point to a maximum of about 30°C, which greatly changes the operating conditions of the fuel gas revaporization equipment, and especially when the atmospheric temperature is low, it is necessary to protect the compressor, etc. I understand. by the way,
When the atmospheric temperature is low, such as in the winter, the maximum output of the turbine increases, but in the summer, the maximum output decreases.
There is no problem of insufficient capacity for the load.
よって、大気温度の低い場合には、大気を加熱して再気
化装置3に導入することが必要になり、また、その場合
の影響は小さいことが分る。Therefore, when the atmospheric temperature is low, it is necessary to heat the atmospheric air and introduce it into the revaporization device 3, and it can be seen that the influence in this case is small.
従って、本発明においては、再気化装置3に流入する大
気をガスタービン等の廃ガスを用いて予め定めた温度以
上に調整制限することがある。Therefore, in the present invention, the atmospheric air flowing into the revaporization device 3 may be adjusted and limited to a temperature above a predetermined temperature using waste gas from a gas turbine or the like.
大気5をガスタービン廃ガス16を用いて、再気化装R
3に流入する空気51の温度を定められた値以上、たと
えばIOc以上に制限する。、空気51の温度を測定し
、これに基すき流量調整弁17の開度を調整する。第1
図の破線はこれを示す。The atmosphere 5 is converted into a re-vaporizer R using gas turbine waste gas 16.
The temperature of the air 51 flowing into the air filter 3 is limited to a predetermined value or higher, for example, IOc or higher. , the temperature of the air 51 is measured, and the opening degree of the plow flow rate regulating valve 17 is adjusted based on the temperature. 1st
The dashed line in the figure indicates this.
大気5を廃ガス16で加熱する場合、種々の方法が考え
られるが、廃カスは酸素含有量が大気に比べ少いから、
大気と廃ガス全直接混合させることによって、燃焼空気
8の酸素含有量が減少し、燃焼時発生する窒素−酸化物
を抑える効果が得られるので有利である。When heating the atmosphere 5 with the waste gas 16, various methods can be considered, but since the waste gas has a lower oxygen content than the atmosphere,
The complete direct mixing of the exhaust gases with the atmosphere is advantageous because the oxygen content of the combustion air 8 is reduced and the nitrogen-oxides generated during combustion are suppressed.
以上の如き廃ガス’16による大気の加熱は、7気温度
がある値以下、たとえば10C以下の場合に行なわれる
。The heating of the atmosphere by the waste gas '16 as described above is carried out when the temperature is below a certain value, for example below 10C.
尚、廃ガスにより液化燃料の再気化全行うことは周知で
あるが、本発明は、廃ガスにより大気を加熱し、それに
よって再気化を行うものであり、全く新期なものである
。また、廃ガスにより圧縮機入口空気の加熱は周知であ
るが、廃ガスにより液化燃料の再気化装置に流入する空
気を加熱することは本発明の全く新期なものであり、再
気化装置の小型化、氷結防止というような新しい効果を
得ることができる。Although it is well known that liquefied fuel is completely revaporized using waste gas, the present invention is completely new in that it heats the atmosphere with waste gas and thereby performs revaporization. Furthermore, although heating the compressor inlet air with waste gas is well known, heating the air flowing into the liquefied fuel revaporization device with waste gas is completely new to the present invention. New effects such as miniaturization and prevention of freezing can be obtained.
【図面の簡単な説明】
第1図は本発明の一実施例であるガスタービン装置の系
統図である。BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a system diagram of a gas turbine device that is an embodiment of the present invention.
Claims (1)
スを再気化する再気化装置を具えたガスタービン装置に
おいて、再気化装置へ流入する空気をガスタービンの廃
ガスで加熱する手段全設置して、定められた温度以下と
ならないよノに制御したことを特徴とするガスタービン
装置。 2、特許請求の範囲第1項において、再気化装置へ流入
する空気をガスタービン廃ガスによって加熱する手段と
して、廃ガスと空気を混合するようにしたことを特徴と
するガスタービン装置、[Claims] 1. In a gas turbine device equipped with a revaporization device that revaporizes liquefied natural gas using air flowing into a gas turbine compressor, the air flowing into the revaporization device is heated with waste gas from the gas turbine. A gas turbine device characterized in that all means are installed to control the temperature so that it does not fall below a predetermined temperature. 2. A gas turbine device according to claim 1, characterized in that the means for heating the air flowing into the revaporization device by the gas turbine waste gas mixes waste gas and air;
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11395282A JPS595834A (en) | 1982-07-02 | 1982-07-02 | Gas turbine plant |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11395282A JPS595834A (en) | 1982-07-02 | 1982-07-02 | Gas turbine plant |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPS595834A true JPS595834A (en) | 1984-01-12 |
Family
ID=14625316
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP11395282A Pending JPS595834A (en) | 1982-07-02 | 1982-07-02 | Gas turbine plant |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS595834A (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| BE1000183A5 (en) * | 1986-02-07 | 1988-07-19 | Westinghouse Electric Corp | Method for increasing yield of generators gas turbine system using gas low fuel calorific. |
| JPS63203495A (en) * | 1987-02-20 | 1988-08-23 | ヤマハ発動機株式会社 | Carburetor freezing preventive device for snow mobile |
| WO2002077515A1 (en) * | 2001-03-06 | 2002-10-03 | Mitsui Engineering & Shipbuilding Co.,Ltd. | Electric power leveling method and methane hydrate cold-heat utilization power generating system in gas supply business |
| JP2007231955A (en) * | 2001-03-06 | 2007-09-13 | Mitsui Eng & Shipbuild Co Ltd | Methane hydrate cold power generation system |
-
1982
- 1982-07-02 JP JP11395282A patent/JPS595834A/en active Pending
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| BE1000183A5 (en) * | 1986-02-07 | 1988-07-19 | Westinghouse Electric Corp | Method for increasing yield of generators gas turbine system using gas low fuel calorific. |
| JPS63203495A (en) * | 1987-02-20 | 1988-08-23 | ヤマハ発動機株式会社 | Carburetor freezing preventive device for snow mobile |
| WO2002077515A1 (en) * | 2001-03-06 | 2002-10-03 | Mitsui Engineering & Shipbuilding Co.,Ltd. | Electric power leveling method and methane hydrate cold-heat utilization power generating system in gas supply business |
| JP2007231955A (en) * | 2001-03-06 | 2007-09-13 | Mitsui Eng & Shipbuild Co Ltd | Methane hydrate cold power generation system |
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