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JPH0233869B2 - - Google Patents
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JPH0233869B2 - - Google Patents

Info

Publication number
JPH0233869B2
JPH0233869B2 JP60060460A JP6046085A JPH0233869B2 JP H0233869 B2 JPH0233869 B2 JP H0233869B2 JP 60060460 A JP60060460 A JP 60060460A JP 6046085 A JP6046085 A JP 6046085A JP H0233869 B2 JPH0233869 B2 JP H0233869B2
Authority
JP
Japan
Prior art keywords
fuel gas
internal combustion
combustion engine
pipe
compressor
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.)
Expired - Lifetime
Application number
JP60060460A
Other languages
Japanese (ja)
Other versions
JPS60216061A (en
Inventor
Michuki Myake
Akira Hoshino
Yoshiaki Watanabe
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.)
Niigata Engineering Co Ltd
Original Assignee
Niigata Engineering Co 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 Niigata Engineering Co Ltd filed Critical Niigata Engineering Co Ltd
Priority to JP60060460A priority Critical patent/JPS60216061A/en
Publication of JPS60216061A publication Critical patent/JPS60216061A/en
Publication of JPH0233869B2 publication Critical patent/JPH0233869B2/ja
Granted legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02MSUPPLYING COMBUSTION ENGINES IN GENERAL WITH COMBUSTIBLE MIXTURES OR CONSTITUENTS THEREOF
    • F02M21/00Apparatus for supplying engines with non-liquid fuels, e.g. gaseous fuels stored in liquid form
    • F02M21/02Apparatus for supplying engines with non-liquid fuels, e.g. gaseous fuels stored in liquid form for gaseous fuels
    • F02M21/0218Details on the gaseous fuel supply system, e.g. tanks, valves, pipes, pumps, rails, injectors or mixers
    • F02M21/0287Details on the gaseous fuel supply system, e.g. tanks, valves, pipes, pumps, rails, injectors or mixers characterised by the transition from liquid to gaseous phase ; Injection in liquid phase; Cooling and low temperature storage
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02DCONTROLLING COMBUSTION ENGINES
    • F02D19/00Controlling engines characterised by their use of non-liquid fuels, pluralities of fuels, or non-fuel substances added to the combustible mixtures
    • F02D19/02Controlling engines characterised by their use of non-liquid fuels, pluralities of fuels, or non-fuel substances added to the combustible mixtures peculiar to engines working with gaseous fuels
    • F02D19/021Control of components of the fuel supply system
    • F02D19/023Control of components of the fuel supply system to adjust the fuel mass or volume flow
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02MSUPPLYING COMBUSTION ENGINES IN GENERAL WITH COMBUSTIBLE MIXTURES OR CONSTITUENTS THEREOF
    • F02M21/00Apparatus for supplying engines with non-liquid fuels, e.g. gaseous fuels stored in liquid form
    • F02M21/02Apparatus for supplying engines with non-liquid fuels, e.g. gaseous fuels stored in liquid form for gaseous fuels
    • F02M21/06Apparatus for de-liquefying, e.g. by heating
    • 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
    • Y02TCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
    • Y02T10/00Road transport of goods or passengers
    • Y02T10/10Internal combustion engine [ICE] based vehicles
    • Y02T10/30Use of alternative fuels, e.g. biofuels

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Engine Equipment That Uses Special Cycles (AREA)
  • Output Control And Ontrol Of Special Type Engine (AREA)

Description

【発明の詳細な説明】 「産業上の利用分野」 この本発明は、ガス燃焼式内燃機、すなわちガ
スタービンおよびエンジンに燃料ガスを供給する
燃料ガス供給装置に関するものである。
DETAILED DESCRIPTION OF THE INVENTION "Field of Industrial Application" The present invention relates to a fuel gas supply device for supplying fuel gas to a gas combustion internal combustion engine, that is, a gas turbine and an engine.

「従来の技術」 一般に、上記ガス燃焼式内燃機における燃料ガ
スは、圧縮機により圧力を高めて内燃機に供給さ
れている。
"Prior Art" Generally, fuel gas in the gas-burning internal combustion engine is supplied to the internal combustion engine after increasing its pressure by a compressor.

第5図は従来の燃料ガス供給装置を示す一例
で、1は圧縮機、2はガス燃焼式の内燃機、3は
この内燃機2に接続された負荷、4は圧力制御装
置、5は圧力制御装置により制御される圧力調整
弁、6は冷却器である。この例では、配管fで供
給され圧縮機1で圧縮された圧縮燃料ガスは、圧
力制御装置4によつて制御され供給管路a,cを
介して所定量が内燃機2に供給される。残りの圧
縮燃料ガスは、圧力調整弁5より戻り管路bに分
岐導出され、冷却器6で冷却され、圧縮機1吸込
側の配管dで供給燃料ガスと混合され、再び圧縮
機1に導かれるようになつていた。
FIG. 5 shows an example of a conventional fuel gas supply system, in which 1 is a compressor, 2 is a gas combustion internal combustion engine, 3 is a load connected to this internal combustion engine 2, 4 is a pressure control device, and 5 is a pressure control device. 6 is a cooler. In this example, compressed fuel gas supplied through pipe f and compressed by compressor 1 is controlled by pressure control device 4, and a predetermined amount of compressed fuel gas is supplied to internal combustion engine 2 via supply pipes a and c. The remaining compressed fuel gas is branched out from the pressure regulating valve 5 to a return pipe b, cooled by a cooler 6, mixed with the supplied fuel gas in a pipe d on the suction side of the compressor 1, and then led to the compressor 1 again. I was starting to feel depressed.

「発明が解決しようとする問題点」 このような従来例においては、圧縮機1から吐
出された燃料ガスは該圧縮機1により高温となる
が、圧縮機1と内燃機2との間の管路で放熱によ
つて燃料ガス温度が低下し、ガス成分の一部が凝
縮液化してミストが出来る。特に外気温が低い場
合や内燃機の起動時、冷えている配管によつてこ
の現象が顕著となる。この発明ミストが同伴する
ことで内燃機の燃料コントロール系統に詰つて
種々のトラブルの原因となつていたり、流量調整
用やシヤツトダウン用等の各種バルブの作動不良
の原因となつていた。
"Problems to be Solved by the Invention" In such a conventional example, the fuel gas discharged from the compressor 1 is heated to a high temperature by the compressor 1, but the pipe line between the compressor 1 and the internal combustion engine 2 The temperature of the fuel gas decreases due to heat radiation, and some of the gas components condense and liquefy, creating mist. This phenomenon is particularly noticeable when the outside temperature is low or when starting up an internal combustion engine, due to cold pipes. When the mist of the present invention is entrained, it clogs the fuel control system of the internal combustion engine, causing various troubles and malfunctioning of various valves for flow rate adjustment, shutdown, etc.

「問題点を解決するための手段」 この発明は上記従来の欠点を解消するために提
案されたもので、その特徴とするところは、圧縮
燃料ガス供給管路の内燃機近傍と圧縮機吸込側と
を結ぶバイパス管路と、内燃機起動前に圧縮燃料
ガスを上記圧縮燃料ガス供給管路から上記バイパ
ス管路に流通させる弁と、上記バイパス管路また
は圧縮機吸込側の該バイパス管路分岐部から上記
圧縮機までの管路に設けられた凝縮液分離手段
と、を設けたガス燃焼式内燃機における燃料ガス
供給装置にある。
"Means for Solving the Problems" This invention was proposed to solve the above-mentioned conventional drawbacks, and is characterized by the fact that the compressed fuel gas supply pipe is located near the internal combustion engine and on the compressor suction side. a bypass pipe connecting the internal combustion engine, a valve that allows compressed fuel gas to flow from the compressed fuel gas supply pipe to the bypass pipe before starting the internal combustion engine, and a valve that flows from the bypass pipe or the bypass pipe branch on the compressor suction side. A fuel gas supply device for a gas combustion internal combustion engine includes a condensate separation means provided in a pipe line leading to the compressor.

「作 用」 内燃機起動前に、圧縮機で圧縮された圧縮燃料
ガスを圧縮燃料ガス供給管路の内燃機近傍からバ
イパス管路を介して圧縮機吸込側へと循環させ
る。該圧縮燃料ガス成分の一部は、上記圧縮燃料
ガス供給管路で放熱によつて凝縮液化しミストが
できるが、該ミストは凝縮液分離手段によつて除
去され、燃料ガスは再び圧縮機に導かれると共
に、上記圧縮燃料ガス供給管路は圧縮燃料ガスに
より加熱される。
"Function" Before starting the internal combustion engine, the compressed fuel gas compressed by the compressor is circulated from the compressed fuel gas supply line near the internal combustion engine to the compressor suction side via the bypass line. A part of the compressed fuel gas component is condensed and liquefied by heat radiation in the compressed fuel gas supply pipe to form a mist, but the mist is removed by the condensate separation means and the fuel gas is returned to the compressor. The compressed fuel gas supply line is heated by the compressed fuel gas.

上記圧縮燃料ガス供給管路が温まり、ミストが
生じなくなると弁を切換え、内燃機に圧縮燃料ガ
スを供給して内燃機を起動させる。
When the compressed fuel gas supply pipe becomes warm and mist is no longer generated, the valve is switched, compressed fuel gas is supplied to the internal combustion engine, and the internal combustion engine is started.

これにより、内燃機の起動の際の燃料系統のト
ラブルを押えることが出来る。
This can prevent troubles in the fuel system when starting the internal combustion engine.

「実施例」 以下、この発明の一実施例を図面に従つて説明
する。
"Embodiment" An embodiment of the present invention will be described below with reference to the drawings.

第1図において、20はミストセパレータ、2
1は容積式、ターボ式、軸流式等の圧縮機、22
は熱交換器、23はアフタクーラ(冷却器)、2
4はドレンセパレータ、25はフイルタ、26は
ガスタービンやガスエンジン等のガス燃焼式の内
燃機、27は負荷、28は内燃機の起動前に使用
するための補助ドレンセパレータである。そして
矢印イのようにガス入口29から供給された燃料
ガスが、ミストセパレータ20、圧縮機21、熱
交換器22、アフタクーラ23、ドレンセパレー
タ4をそれぞれ経て送られるように配管され、さ
らに、ドレンセパレータ24の下流の配管Aは、
ミストセパレータ20に戻る戻り配管Bと、内燃
機26に熱交換器22およびフイルタ25を経て
送られる内燃機系統の配管C(このうち熱交換器
22の上流の配管C1、下流の配管をC2とする)
とに分岐配管されている。また、上記補助ドレン
セパレータ28が介装されたバイパス配管Dが、
上記配管C2のフイルタ25上流側近傍とミスト
セパレータ20上流側近傍との間に配管されてい
る。このバイパス配管Dと上記配管C2との分岐
部には、燃料ガスを配管C2からバイパス配管D
に流通させる弁として配管C2の分岐点下流側に
バルブ34が、またバイパス配管Dにバルブ35
が設けられている。また、ドレンセパレータ24
の下流の配管Aの分岐する直前の部分およびミス
トセパレータ20にはガスの圧力を検知してその
圧力に応じて制御信号を出す圧力制御装置30,
31がそれぞれ設けられ、前記配管Bには圧力調
整弁32が設けられている。この圧力調整弁32
は、通常は配管Aの圧力制御装置30によつて制
御されるが、ミストセパレータ20内の圧力(す
なわち、圧縮機21の吸込圧力)が異常に低下し
たとき、選択制御装置33によつて切替えられて
ミストセパレータ20側の圧力制御装置31の制
御信号により作動するようになつている。
In FIG. 1, 20 is a mist separator;
1 is a positive displacement type, turbo type, axial type, etc. compressor; 22
is a heat exchanger, 23 is an aftercooler, 2
4 is a drain separator, 25 is a filter, 26 is a gas combustion type internal combustion engine such as a gas turbine or gas engine, 27 is a load, and 28 is an auxiliary drain separator for use before starting the internal combustion engine. As shown by arrow A, the fuel gas supplied from the gas inlet 29 is piped so as to be sent through the mist separator 20, the compressor 21, the heat exchanger 22, the aftercooler 23, and the drain separator 4. The downstream pipe A of 24 is
A return pipe B returns to the mist separator 20, and a pipe C of the internal combustion engine system that is sent to the internal combustion engine 26 via the heat exchanger 22 and the filter 25 (of these, the upstream pipe C 1 of the heat exchanger 22 and the downstream pipe C 2 do)
There is branch piping. Moreover, the bypass pipe D in which the auxiliary drain separator 28 is interposed is
The pipe C 2 is installed between the upstream side of the filter 25 and the upstream side of the mist separator 20 . At the branch point between this bypass pipe D and the above-mentioned pipe C2 , fuel gas is connected from pipe C2 to bypass pipe D.
There is a valve 34 on the downstream side of the branch point of pipe C2 , and a valve 35 on the bypass pipe D.
is provided. In addition, the drain separator 24
A pressure control device 30 that detects the gas pressure and outputs a control signal in accordance with the pressure is installed in the downstream portion of the pipe A immediately before branching and the mist separator 20.
31 are respectively provided, and the pipe B is provided with a pressure regulating valve 32. This pressure regulating valve 32
is normally controlled by the pressure control device 30 of the pipe A, but is switched by the selection control device 33 when the pressure inside the mist separator 20 (i.e., the suction pressure of the compressor 21) drops abnormally. The mist separator 20 is operated by a control signal from a pressure control device 31 on the mist separator 20 side.

次に上述の燃料ガス供給装置の運転について説
明する。
Next, the operation of the above-mentioned fuel gas supply device will be explained.

(1) まず、内燃機26の起動前に内燃機26の手
前のバルブ34を閉、補助ドレンセパレータ2
8側のバルブ35を開とし圧縮機21を運転す
る。
(1) First, before starting the internal combustion engine 26, close the valve 34 in front of the internal combustion engine 26, and close the auxiliary drain separator 2.
The valve 35 on the 8 side is opened and the compressor 21 is operated.

(2) ガス入口29における燃料ガスは通常、温度
は常温、圧力は1.0〜7.0Kg/cm2A(絶対圧)で
ある。
(2) The temperature of the fuel gas at the gas inlet 29 is normally room temperature and the pressure is 1.0 to 7.0 Kg/cm 2 A (absolute pressure).

(3) ミストセパレータ20により通常ミストの約
90%が除去される。
(3) The mist separator 20 allows the normal mist to
90% removed.

(4) 圧縮機21の吸込口においては、ミストセパ
レータ20および配管系の圧力損失により、圧
力がガス入口29での圧力より、通常約0.2〜
1.0Kg/cm2低くなる。
(4) At the suction port of the compressor 21, the pressure is usually about 0.2 to 0.2 to less than the pressure at the gas inlet 29 due to pressure loss in the mist separator 20 and piping system.
1.0Kg/ cm2 lower.

(5) 圧縮機21の吐出側では、吐出圧力は、通常
10〜16Kg/cm2A(これは、内燃機26の要求ガ
ス圧力に圧縮機21と内燃機との間の配管系の
圧力損失を加えた大きさの吐出圧力である)、
吐出温度は90〜130℃である。
(5) On the discharge side of the compressor 21, the discharge pressure is normally
10 to 16 Kg/cm 2 A (this is the discharge pressure equal to the required gas pressure of the internal combustion engine 26 plus the pressure loss of the piping system between the compressor 21 and the internal combustion engine),
The discharge temperature is 90-130°C.

なお、吐出温度は次式により定まる。 Note that the discharge temperature is determined by the following equation.

但し、可逆断熱式圧縮の場合(容積式圧縮
機) 但し、ポリトロープ圧縮の場合(ターボ式圧
縮機) ここで、Td:吐出温度(〓) Ts:吸込温度(〓) Pd:吐出圧力(Kg/cm2A) Ps:吸込圧力(Kg/cm2A) K:ガス定数比Cp/Cv Cp:定圧比熱 Cv:定容比熱 n:ポリトロープ変化の場合の指数 上記の(),()式から明らかなように、
圧縮機21の吐出圧力Pdを下げれば吐出温度
Tdも下がる。そして、圧縮機21の吐出圧力
Pdは圧力制御装置30の設定値を下げること
によつて下げることができる。
However, in the case of reversible adiabatic compression (positive displacement compressor) However, in the case of polytropic compression (turbo compressor), Td: Discharge temperature (〓) Ts: Suction temperature (〓) Pd: Discharge pressure (Kg/cm 2 A) Ps: Suction pressure (Kg/cm 2 A) ) K: Gas constant ratio Cp/Cv Cp: Specific heat at constant pressure Cv: Specific heat at constant volume n: Index in case of polytropic change As is clear from the above equations () and (),
If the discharge pressure Pd of the compressor 21 is lowered, the discharge temperature
Td also decreases. And the discharge pressure of the compressor 21
Pd can be lowered by lowering the set value of the pressure control device 30.

(6) 熱交換器22においては、圧縮機21から出
た高温圧縮燃料ガスが内燃機系統の配管Cを流
れる低温圧縮燃料ガスに熱エネルギを与えてこ
れを加熱する。なお、この熱交換の現象につい
ては後でさらに詳しく述べる。
(6) In the heat exchanger 22, the high-temperature compressed fuel gas discharged from the compressor 21 gives thermal energy to the low-temperature compressed fuel gas flowing through the pipe C of the internal combustion engine system to heat it. Note that this heat exchange phenomenon will be described in more detail later.

(7) 熱交換器22において少し冷やされた高温圧
縮燃料ガスはアフタクーラ23において常温近
くまで再度冷却される。このとき、圧縮燃料ガ
ス中に含まれる一部の成分は、温度が下がるこ
とによて凝縮液化する。
(7) The high temperature compressed fuel gas that has been slightly cooled in the heat exchanger 22 is cooled again to near room temperature in the aftercooler 23. At this time, some components contained in the compressed fuel gas are condensed and liquefied as the temperature decreases.

(8) 冷却された圧縮燃料ガスに飛沫同伴した凝縮
液はドレンセパレータ4で分離除去される。な
お、上記クーラの種類によつては、この凝縮液
はクーラのドレン排出口により排出される。
(8) The condensate entrained in the cooled compressed fuel gas is separated and removed by the drain separator 4. Note that, depending on the type of the cooler, this condensed liquid is discharged through a drain outlet of the cooler.

(9) なおガス入口29からドレンセパレータ24
の下流の配管Aまでの間には、圧縮機21の容
量分だけの圧縮燃料ガスが流れている。
(9) Furthermore, from the gas inlet 29 to the drain separator 24
Compressed fuel gas corresponding to the capacity of the compressor 21 flows between the downstream pipe A and the pipe A.

(10) 圧力制御装置30によつて圧力を検出して、
その検知した圧力に応じて圧力調整弁32の開
度が調整され、内燃機系統の配管Cに送られる
圧縮燃料ガスの圧力が一定に保たれ、内燃機系
統の配管Cには、バイパス配管Dに流通する圧
縮燃料ガス分だけが流れる。
(10) Detecting the pressure by the pressure control device 30,
The opening degree of the pressure regulating valve 32 is adjusted according to the detected pressure, and the pressure of the compressed fuel gas sent to the pipe C of the internal combustion engine system is kept constant, and the pipe C of the internal combustion engine system is distributed to the bypass pipe D. Only the amount of compressed fuel gas that flows flows.

そして、熱交換器22に入る前には飽和状態
又は過飽和状態にあつた圧縮燃料ガスは、熱交
換器22によつて加熱されて過熱圧縮燃料ガス
となり配管C2を流通する。配管C2を流通して
いる間に、圧縮燃料ガスは該配管C2を温める
と共に該圧縮燃料ガスの一部は凝冷液化しミス
トとなる。ミストを同伴した圧縮燃料ガスは配
管C2からバイパス配管に流入し、補助ドレン
セパレータ28で補助的にミストが除かれた
後、ミストセパレータ20上流のガス入口29
に戻る。そしてミストセパレータ20によつて
さらにミストが除かれ再び圧縮機21に導入さ
れる。
The compressed fuel gas, which was in a saturated or supersaturated state before entering the heat exchanger 22, is heated by the heat exchanger 22 and becomes superheated compressed fuel gas, which flows through the pipe C2 . While flowing through the pipe C 2 , the compressed fuel gas warms the pipe C 2 and a portion of the compressed fuel gas is condensed and liquefied to become mist. The compressed fuel gas accompanied by the mist flows into the bypass pipe from the pipe C 2 , and after the mist is auxiliary removed by the auxiliary drain separator 28 , the gas inlet 29 upstream of the mist separator 20
Return to Then, the mist is further removed by the mist separator 20 and introduced into the compressor 21 again.

(11) 内燃機系統の配管Cに送られる圧縮燃料ガス
は上述のようにバイパス配管Dに流れる分に見
合う量だけしか流れないため、余割分の圧縮燃
料ガスは圧力調整弁32及び戻り配管Bを経て
ガス入口29に戻る。
(11) As mentioned above, the compressed fuel gas sent to pipe C of the internal combustion engine system only flows in an amount corresponding to the amount flowing to bypass pipe D, so the remaining amount of compressed fuel gas is sent to pressure regulating valve 32 and return pipe B. and returns to the gas inlet 29.

(12) 上述のように圧縮燃料ガスを圧縮機21、配
管C2、バイパス配管D及びミストセパレータ
20を経て圧縮機21へと循環し配管C2が温
まると、内燃機26の手前のバルブ34を開、
補助ドレンセパレータ28側のバルブ35を閉
として上記過熱圧縮燃料ガスを内燃機26に供
給する。内燃機系統の配管Cには、内燃機26
の負荷が要求する分だけ燃料ガスが分岐して送
られる。
(12) As mentioned above, when the compressed fuel gas is circulated to the compressor 21 via the compressor 21, the pipe C 2 , the bypass pipe D and the mist separator 20 and the pipe C 2 becomes warm, the valve 34 in front of the internal combustion engine 26 is closed. Open,
The valve 35 on the side of the auxiliary drain separator 28 is closed, and the superheated compressed fuel gas is supplied to the internal combustion engine 26. The internal combustion engine 26 is connected to the piping C of the internal combustion engine system.
The fuel gas is branched and sent in the amount required by the load.

また、内燃機系統の配管Cに送られる圧縮燃料
ガスは内燃機26の負荷27に見合う量だけしか
流れないため、余剰分の圧縮燃料ガスは圧力調整
弁32及び戻り配管Bを経てガス入口29に戻
る。
Further, since the compressed fuel gas sent to the pipe C of the internal combustion engine system flows only in an amount corresponding to the load 27 of the internal combustion engine 26, the surplus compressed fuel gas returns to the gas inlet 29 via the pressure regulating valve 32 and the return pipe B. .

なお、戻り配管Bからガス入口29に戻る燃料
ガスはアフタクーラ23を経たものでなければな
らない。なぜならば、圧縮機21が容積式のもの
であつても、完全な可逆断熱変化により圧縮され
るのではなく、圧縮機の摩擦熱などにより実際に
は余分に加熱されるため、圧縮された高温ガスを
圧力調整弁32で断熱膨張させたとしても、もと
の供給ガス温度まで下がらず、したがつて、この
戻りガスが循環していると仮に考えると、そのガ
スは圧縮機21により相乗的に加熱され、その結
果圧縮機21の吐出ガスの温度が上昇していき機
械的問題が生じるからである。
Note that the fuel gas returning from the return pipe B to the gas inlet 29 must pass through the aftercooler 23. This is because, even if the compressor 21 is a positive displacement type, the compression is not due to a complete reversible adiabatic change, but is actually heated excessively due to the frictional heat of the compressor, so the compressed high temperature Even if the gas is adiabatically expanded by the pressure regulating valve 32, the temperature of the supplied gas will not drop to the original supply gas temperature. This is because the temperature of the gas discharged from the compressor 21 increases, causing mechanical problems.

また、ミストセパレータ20側の圧力制御装置
31は、ドレンセパレータ24の下流の配管Aの
圧力制御装置30と同様に制御信号を出してお
り、通常は選択制御装置33によつて無視されて
いるが、ガス入口29の燃料ガスの供給量が減少
して圧縮機21の吸込圧力が一定値以下に下つた
ときには、選択制御装置33によつて切替えがな
され、圧力調整弁32は、ミストセパレータ20
側の圧力制御装置31によつてのみ制御される。
この場合、配管Aの圧力制御装置30は無視さ
れ、圧縮機21の吐出側の圧縮燃料ガスを吸込側
に戻して圧縮機21の吸込側の圧力低下を防ぐよ
うに、圧力調整弁32が開となる制御がなされ
る。これは、圧縮機21の吸込圧力が低下した場
合、圧縮機21に異常な影響を与えて故障の原因
となるからである。すなわち内燃機26への供給
より、圧縮機21の保護を優先させるためであ
る。この様に入口29の供給量が減つて内燃機系
統の配管Cにおける圧力が一定値以下に低下した
ときには、図示しない別の燃料系統(通常は液体
燃料)に切り替えるか、あるいは内燃機26の運
転を止める。
Further, the pressure control device 31 on the mist separator 20 side outputs a control signal in the same way as the pressure control device 30 in the pipe A downstream of the drain separator 24, and although it is normally ignored by the selection control device 33, When the amount of fuel gas supplied to the gas inlet 29 decreases and the suction pressure of the compressor 21 falls below a certain value, the selection control device 33 switches the pressure regulating valve 32 to the mist separator 20.
It is controlled only by the side pressure control device 31.
In this case, the pressure control device 30 of the pipe A is ignored, and the pressure regulating valve 32 is opened so as to return the compressed fuel gas on the discharge side of the compressor 21 to the suction side and prevent a pressure drop on the suction side of the compressor 21. The following control is performed. This is because if the suction pressure of the compressor 21 decreases, it will have an abnormal effect on the compressor 21 and cause it to malfunction. In other words, this is to prioritize protection of the compressor 21 over supply to the internal combustion engine 26. In this way, when the supply amount at the inlet 29 decreases and the pressure in the pipe C of the internal combustion engine system drops below a certain value, either switch to another fuel system (not shown) (usually liquid fuel) or stop the operation of the internal combustion engine 26. .

次に、前述の(6)の項で述べた本実施例の熱交換
器22における熱交換の現象について述べる。
Next, the phenomenon of heat exchange in the heat exchanger 22 of this embodiment described in the above section (6) will be described.

一般に熱交換器における交換熱量Qは次式で定
まる。
Generally, the amount of heat exchanged Q in a heat exchanger is determined by the following equation.

Q=U×A×△tm ……() U:総括伝熱係数 A:伝熱面積(一定) △tm:対数平均温度差 △tm:△t1−△t2/loge△t1/△t2……() △t1=T2−t1 △t2=T1−t2 T1:加熱流体の熱交換器入口における温度 T2:加熱流体の熱交換器出口における温度 t1:被加熱流体の熱交換器入口における温度 t2:被加熱流体の熱交換器出口における温度 被加熱流体の流量(すなわち、内燃機系統の配
管Cにおける流量)が減り、ガス流速が減ると、
総括伝熱係数Uが少なくなる。また、被加熱流体
の出口における温度t2は上昇するが、加熱流体と
被加熱流体の温度差、すなわちT1−t2(=△t2
が小さくなり、()式における分子の数値は大
きくなるが、それにも増して分母の数値の方が大
きくなるので対数平均温度差△tmは小くなる
(このことは、()式において数学的演算により
直ちに導かれることである)。したがつて、被加
熱流体の流量Gが小さくなると熱交換量Qも小さ
くなる。
Q = U × A × △tm ... () U: Overall heat transfer coefficient A: Heat transfer area (constant) △tm: Logarithm mean temperature difference △tm: △t 1 −△t 2 /loge△t 1 /△ t 2 ... () △t 1 = T 2 −t 1 △t 2 = T 1t 2 T 1 : Temperature of heating fluid at the inlet of the heat exchanger T 2 : Temperature of the heating fluid at the exit of the heat exchanger t 1 : Temperature of the heated fluid at the heat exchanger inlet t 2 : Temperature of the heated fluid at the heat exchanger outlet When the flow rate of the heated fluid (i.e., the flow rate in pipe C of the internal combustion engine system) decreases and the gas flow rate decreases,
The overall heat transfer coefficient U decreases. Also, although the temperature t 2 at the outlet of the heated fluid increases, the temperature difference between the heated fluid and the heated fluid, that is, T 1 − t 2 (=△t 2 )
becomes smaller, and the numerical value of the numerator in equation () becomes larger, but the numerical value of the denominator becomes larger, so the logarithmic average temperature difference △tm becomes smaller (this means that mathematically, in equation (), (This is immediately derived by calculation). Therefore, as the flow rate G of the fluid to be heated decreases, the amount of heat exchange Q also decreases.

ところで、一定の伝熱面積を有する熱交換器に
おいて移動する熱量として、加熱される被加熱流
体の温度上昇は次式で定まる。
By the way, as the amount of heat transferred in a heat exchanger having a fixed heat transfer area, the temperature rise of the heated fluid is determined by the following equation.

△t=Q/G×Cp G:被加熱流体の流量 Cp:被加熱流体の比熱 △t:被加熱流体の温度上昇 ここにおいて、前述した如く被加熱流体の流量
Gが小さくなつても、熱交換量Qも小さくなるの
で、被加熱流体の温度上昇△tはそれ程大きくな
らない。
△t = Q/G Since the exchange amount Q also becomes small, the temperature rise Δt of the heated fluid does not become so large.

すなわち、内燃機26の負荷が減少して、内燃
機系統の配管Cに流れるガス量が減つても(な
お、その限度は、一般に定格負荷時の流量の約40
%である)、この熱交換器22において加熱しす
ぎることがない。このように本実施例において
は、熱交換器22の加熱流体として圧縮器の吐出
燃料ガスを用いることにより、この熱交換器22
は、加熱しすぎることのない自己調整能をもつも
のとなつており、内燃機26へ送る燃料ガスの温
度上昇を許容値以内に収めることが可能となつて
いる。
In other words, even if the load on the internal combustion engine 26 decreases and the amount of gas flowing into the piping C of the internal combustion engine system decreases (the limit is generally about 40% of the flow rate at rated load).
%), the heat exchanger 22 will not overheat. In this way, in this embodiment, by using the fuel gas discharged from the compressor as the heating fluid of the heat exchanger 22, the heat exchanger 22
has a self-adjusting ability to prevent overheating, making it possible to keep the temperature rise of the fuel gas sent to the internal combustion engine 26 within an allowable value.

さらに、上記温度上昇が許容値を越えるケース
がある場合でも、内燃機26が必要とする圧力範
囲(通常約8〜14Kg/cm2G(ゲージ圧))で吐出圧
力を下げることにより圧縮機21の吐出温度を下
げて、内燃機26へ送る燃料ガスの温度を許容値
以内に収めることができる。この状況を詳しく説
明すれば、前述した()式、()式より明ら
かなとおり、圧縮機21の吐出圧力Pdを下げれ
ば、吐出温度Tdも下がる。そして圧縮機21の
吐出圧力Pdを下げることは圧力制御装置30の
設定値を下げることによつて行うことができるの
で、圧力制御装置30の設定値を内燃機26が必
要とする圧力範囲内で低く設定することによつて
圧縮機21の吐出温度を下げることができ、その
結果として、内燃機系統の配管C2のガス温度を
下げることができる。
Furthermore, even if the temperature rise exceeds the allowable value, the pressure of the compressor 21 can be reduced by lowering the discharge pressure within the pressure range required by the internal combustion engine 26 (usually approximately 8 to 14 kg/cm 2 G (gauge pressure)). By lowering the discharge temperature, the temperature of the fuel gas sent to the internal combustion engine 26 can be kept within an allowable value. To explain this situation in detail, as is clear from the above-mentioned equations () and (), if the discharge pressure Pd of the compressor 21 is lowered, the discharge temperature Td will also be lowered. Since the discharge pressure Pd of the compressor 21 can be lowered by lowering the setting value of the pressure control device 30, the setting value of the pressure control device 30 can be lowered within the pressure range required by the internal combustion engine 26. By setting, the discharge temperature of the compressor 21 can be lowered, and as a result, the gas temperature in the pipe C2 of the internal combustion engine system can be lowered.

そして、圧力制御装置30の設定値を変えるこ
とは、手動で行つてもよい。このような設定値の
変更は、夏期と冬期とでガス入口29から供給さ
れる燃料ガスの温度に著しい差がある場合などに
行うとよい。又、第2図のように、内燃機系統の
配管C2に、温度を検知してその検知した温度に
応じた制御信号を出す温度制御装置36を設け、
この制御信号によつて配管Aの圧力制御装置30
の設定値を変えるようにし、このようなカスケー
ド制御によつて圧力制御装置30の設定値の変更
を自動的に行うようにしてもよい。
The set value of the pressure control device 30 may be changed manually. Such a change in the set value is preferably performed when there is a significant difference in the temperature of the fuel gas supplied from the gas inlet 29 between summer and winter. Further, as shown in FIG. 2, a temperature control device 36 is installed in the pipe C2 of the internal combustion engine system to detect the temperature and output a control signal according to the detected temperature.
By this control signal, the pressure control device 30 of pipe A
The setting value of the pressure control device 30 may be changed automatically by such cascade control.

以上の様にして内燃機26に許容値以内の温度
でミストのない過熱圧縮燃料ガスを供給すること
ができる。
As described above, superheated compressed fuel gas without mist can be supplied to the internal combustion engine 26 at a temperature within the permissible value.

上記第1図及び第2図で示した実施例では、本
発明の圧縮燃料ガス供給管路及びバイパス管路
が、それぞれ配管A,C及びバイパス配管Dで構
成され、本発明の圧縮燃料ガス供給管路からバイ
パス管路に流通させる弁がバルブ34,35で構
成されている。
In the embodiment shown in FIGS. 1 and 2 above, the compressed fuel gas supply line and the bypass line of the present invention are respectively constituted by pipes A and C and bypass pipe D, and the compressed fuel gas supply line and bypass line of the present invention Valves 34 and 35 are configured to allow the flow from the pipeline to the bypass pipeline.

なお、バイパス配管Dに設けられている補助ド
レンセパレータ28は、ミストセパレータ20の
能力が十分にあれば不要である。
Note that the auxiliary drain separator 28 provided in the bypass pipe D is unnecessary if the mist separator 20 has sufficient capacity.

第3図は、他の具体的な実施例を示すもので、
定格2500kwのガスタービン40,40の2基に
燃料を供給するものである。そして、吸込圧力
1.033Kg/cm2Aから吐出圧力17.3Kg/cm2Gに圧縮
するために2段の往復動圧縮機41,42を設
け、中間クーラ(冷却器)43、中間ミストセパ
レータ44を設けている。中間クーラ43、およ
びアフタクーラ23は大気温度が最高45℃の条件
における空冷式である。また、熱交換器22の容
量はガスタービン定格2500kw2台分とし、約
10000kcal/Hの交換熱容量を有する伝熱面積14
m2の二重管式熱交換器を用いている。なお、第1
図と共通する部分については同一符号を付して説
明を省略する。また使用する燃料ガスの性状は次
のものとする。
FIG. 3 shows another specific example.
It supplies fuel to two gas turbines 40 and 40 with a rating of 2500kw. and suction pressure
Two-stage reciprocating compressors 41 and 42 are provided to compress from 1.033 Kg/cm 2 A to a discharge pressure of 17.3 Kg/cm 2 G, and an intermediate cooler 43 and an intermediate mist separator 44 are provided. The intermediate cooler 43 and the aftercooler 23 are air-cooled when the atmospheric temperature is at a maximum of 45°C. In addition, the capacity of the heat exchanger 22 is equivalent to two gas turbines with a rating of 2500kw, and is approximately
Heat transfer area 14 with exchange heat capacity of 10000kcal/H
A double pipe heat exchanger of m 2 is used. In addition, the first
Portions common to those in the figures are designated by the same reference numerals, and description thereof will be omitted. The properties of the fuel gas used shall be as follows.

成分 1段目圧縮機41入口におけるモル比
(%) メタン 15.82 エタン 13.84 プロパン 22.26 イソブタン 6.26 ノルマルブタン 13.99 ノルマルペンタン 5.50 ヘキサン 4.40 ヘプタン 3.69 水蒸気 3.14 硫化水素 3.95 窒 素 0.87 炭酸ガス 1.34 合 計 100% 上記燃料ガスを用いた場合の結果を示すと、第
3図の各段階に記す通りとなり、ガスタービン4
0に65℃の燃料ガスを供給することができた。
Component Molar ratio (%) at the inlet of the first stage compressor 41 Methane 15.82 Ethane 13.84 Propane 22.26 Isobutane 6.26 Normal butane 13.99 Normal pentane 5.50 Hexane 4.40 Heptane 3.69 Water vapor 3.14 Hydrogen sulfide 3.95 Nitrogen 0.87 Carbon dioxide 1.34 Total 100% Above fuel gas The results when using gas turbine 4 are as shown in each stage of Fig. 3.
It was possible to supply fuel gas at 65°C to 0.

以上の実施例において、アフタクーラ23の容
量は、後述の第4図に示す如く外部熱源によるヒ
ータ50を用いたものと較べ、熱交換器22の容
量10000k cal/H相当分だけ小さくすることが可
能となつた。
In the above embodiment, the capacity of the aftercooler 23 can be reduced by the capacity of the heat exchanger 22, which is 10000 kcal/H, compared to the case where a heater 50 using an external heat source is used as shown in FIG. 4, which will be described later. It became.

また、ガスタービン40側への燃料ガス供給量
はガスタービン1台無負荷運転の時に最少となる
が、このときガスタービン40へ送られる燃料ガ
スは熱交換器22において最高に加熱され、その
ときのガス温度は77℃であつた。この温度はガス
タービンへ送られる燃料ガスとしては許容される
範囲内のものである。
Further, the amount of fuel gas supplied to the gas turbine 40 side is at its minimum when one gas turbine is in no-load operation, but the fuel gas sent to the gas turbine 40 at this time is heated to the maximum in the heat exchanger 22, and at that time The gas temperature was 77°C. This temperature is within an acceptable range for fuel gas sent to a gas turbine.

またこれによつて起動のはじめからミストのな
い過熱燃料ガスを供給することができたので、ガ
スタービンの起動の際の燃料系統のトラブルをお
さえることができ、さらにガスタービンのオーバ
ホールの行なう時期を通常10%程度のばしても問
題なく、かつ運転中のトラブル頻度は約半分に減
つた。
This also makes it possible to supply mist-free superheated fuel gas from the beginning of startup, which prevents troubles in the fuel system when starting up the gas turbine, and also helps reduce the timing of overhauling the gas turbine. There was no problem even if the amount of fuel was increased by about 10%, and the frequency of troubles during driving was reduced by about half.

以上の実施例については、圧縮機21の吐出燃
料ガスを加熱流体とする熱交換器22を使用した
例を示したが、これに代えて蒸気等の加熱流体又
は電気を熱源とする外部熱源をもちいてもよい。
In the above embodiment, an example was shown in which the heat exchanger 22 uses the discharged fuel gas of the compressor 21 as the heating fluid, but instead of this, an external heat source using heating fluid such as steam or electricity as the heat source is used. You can also use it.

第4図は、加熱手段として外部熱源によるヒー
タ50をもちいた実施例である。なお、第1図と
共通する部分については同一符号を付して説明を
省略する。
FIG. 4 shows an embodiment in which a heater 50 using an external heat source is used as the heating means. Note that parts common to those in FIG. 1 are denoted by the same reference numerals, and explanations thereof will be omitted.

第4図において矢印イのようにガス入口29か
ら供給された燃料ガスが、ミストセパレータ2
0、圧縮機21、アフタクーラ23、ドレンセパ
レータ24をそれぞれ経て送られるように配置さ
れ、さらに、ドレンセパレータ24の下流の配管
Aは、ミストセパレータ20に戻る戻り配管B
と、内燃機26にヒータ50を経て送られる内燃
機系統の配管Cとに分岐配管されている。また、
上記配管Cの内燃機26近傍とミストセパレータ
20上流側との間にバイパス配管Dが設けられて
いる。さらに、ドレンセパレータ24の下流の配
管Aの分岐点とヒータ50の間の配管Cには圧力
制御装置30が設けられ、ヒータ50と内燃機2
6の間の配管Cには温度制御装置51が設けられ
ている。
In FIG. 4, the fuel gas supplied from the gas inlet 29 as indicated by arrow A flows into the mist separator 2.
0, the compressor 21, the aftercooler 23, and the drain separator 24, and the pipe A downstream of the drain separator 24 is connected to the return pipe B returning to the mist separator 20.
and a pipe C of the internal combustion engine system that is sent to the internal combustion engine 26 via the heater 50. Also,
A bypass pipe D is provided between the pipe C near the internal combustion engine 26 and the upstream side of the mist separator 20. Furthermore, a pressure control device 30 is provided in the pipe C between the branch point of the pipe A downstream of the drain separator 24 and the heater 50.
A temperature control device 51 is provided in the pipe C between the two.

この温度制御装置51によつて内燃機26にお
くられる燃料ガスの温度を常時検出しながらヒー
タ50の蒸気等の加熱流体供給配管52に設けら
れた流量調整弁53を制御し、ミストのない過熱
燃料ガスを内燃機26に供給するようにするので
あるが、起動初期には配管Cが冷えているのでど
うしてもミストが生ずる。そこで内燃機26の起
動前に内燃機26の手前のバルブ34を閉、バイ
パス配管Dのバルブ35を開とし圧縮機21を運
転して燃料ガスを循環させ、配管Cを温める。配
管Cが温まり、ミストが生じなくなるとバルブ3
4を開、バルブ35を閉とすると共に内燃機26
を起動し通常運転に入る。通常運伝後の過熱の程
度はヒータ50から内燃機26までの配管Cの長
さ及び外気温によつてことなるが、一般的には供
給燃料ガスの露点プラス5℃〜20℃に加熱すれば
十分である。このヒータ50の加熱によりミスト
が内燃機26に流入しないので内燃機の燃焼状態
を長期に安定させることができる。
This temperature control device 51 constantly detects the temperature of the fuel gas sent to the internal combustion engine 26 and controls the flow rate adjustment valve 53 provided in the heating fluid supply pipe 52 such as steam of the heater 50, thereby controlling the temperature of the superheated fuel gas without mist. Gas is supplied to the internal combustion engine 26, but since the pipe C is cold in the initial stage of startup, mist is inevitably generated. Therefore, before starting the internal combustion engine 26, the valve 34 in front of the internal combustion engine 26 is closed, the valve 35 of the bypass pipe D is opened, the compressor 21 is operated, the fuel gas is circulated, and the pipe C is warmed. When piping C warms up and no mist is generated, valve 3
4 is opened, the valve 35 is closed, and the internal combustion engine 26 is opened.
Start up and enter normal operation. The degree of overheating after normal operation varies depending on the length of the pipe C from the heater 50 to the internal combustion engine 26 and the outside temperature, but in general, if the fuel gas is heated to 5 to 20 degrees Celsius above the dew point of the supplied fuel gas. It is enough. The heating of the heater 50 prevents mist from flowing into the internal combustion engine 26, so that the combustion state of the internal combustion engine can be stabilized for a long period of time.

なお、54は加熱流体の戻り配管である。 Note that 54 is a return pipe for heating fluid.

以上の実施例では、圧縮機の下流側に燃料ガス
を加熱する手段を設けた場合について述べたが、
第5図で示した燃料ガス加熱手段のない従来の燃
料ガス供給装置に本発明を適用してもよいのは無
論である。
In the above embodiment, a case was described in which a means for heating the fuel gas was provided downstream of the compressor.
It goes without saying that the present invention may be applied to the conventional fuel gas supply device without fuel gas heating means shown in FIG.

「発明の効果」 以上説明したように、この発明の燃料ガス供給
装置によれば圧縮燃料ガス供給管路の内燃機近傍
と圧縮機吸込側とを結ぶバイパス管路と、内燃機
起動前に圧縮燃料ガスを上記圧縮燃料ガス供給管
路から上記バイパス管路に流通させる弁と、上記
バイパス管路または圧縮機吸込側の該バイパス管
路分岐部から上記圧縮機までの管路に設けられた
凝縮液分離手段とを設けたからたとえ起動の際、
圧縮燃料ガス供給管路が冷えていて燃料ガスの一
部がミストとなつても、バイパス管路を介して燃
料ガスを循環せられ圧縮燃料ガス供給管路を温め
ることができるので、内燃機に流入する燃料ガス
にはミストがなく内燃機起動の際の燃料系統のト
ラブルを完全に押えることができ、かつ定期点検
時における燃料ノズル等の清掃が軽減されその部
品交換も少なくなるという顕著な効果がある。
"Effects of the Invention" As explained above, according to the fuel gas supply device of the present invention, a bypass pipe connecting the vicinity of the internal combustion engine of the compressed fuel gas supply pipe and the compressor suction side and a compressed fuel gas a valve that allows the compressed fuel gas to flow from the compressed fuel gas supply pipe to the bypass pipe, and a condensate separator provided in the bypass pipe or a pipe from the bypass pipe branch on the compressor suction side to the compressor. Because we have provided means, even when starting up,
Even if the compressed fuel gas supply pipe is cold and some of the fuel gas turns into mist, the fuel gas is circulated through the bypass pipe and can warm the compressed fuel gas supply pipe, so it will not flow into the internal combustion engine. There is no mist in the fuel gas, which completely eliminates fuel system troubles when starting an internal combustion engine, and has the remarkable effect of reducing the need to clean fuel nozzles and other parts during periodic inspections, reducing the need to replace parts. .

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

第1図は本発明の一実施例を示すシステム図、
第2図は他の実施例を示すシステム図、第3図は
さらに他の実施例を示すシステム図、第4図はさ
らに他の実施例を示すシステム図、第5図は従来
の燃料ガス供給装置のシステム図である。 20……ミストセパレータ(凝縮液分離手段)、
21……圧縮機、26……内燃機、29……ガス
入口(圧縮機吸込側)、34,35……バルブ
(弁)、A,C……配管(圧縮燃料ガス供給管路)。
FIG. 1 is a system diagram showing an embodiment of the present invention;
Fig. 2 is a system diagram showing another embodiment, Fig. 3 is a system diagram showing yet another embodiment, Fig. 4 is a system diagram showing still another embodiment, and Fig. 5 is a conventional fuel gas supply. FIG. 2 is a system diagram of the device. 20...mist separator (condensate separation means),
21...Compressor, 26...Internal combustion engine, 29...Gas inlet (compressor suction side), 34, 35...Valve (valve), A, C...Piping (compressed fuel gas supply pipe).

Claims (1)

【特許請求の範囲】[Claims] 1 燃料ガスを圧縮して内燃機に送る燃料ガス供
給装置において、圧縮燃料ガス供給管路の内燃機
近傍と圧縮機吸込側とを結ぶバイパス管路と、内
燃機起動前に圧縮燃料ガスを上記圧縮燃料ガス供
給管路から上記バイパス管路に流通させる弁と、
上記バイパス管路または圧縮機吸込側の該バイパ
ス管路分岐部から上記圧縮機までの管路に設けら
れた凝縮液分離手段とを設けたことを特徴とする
ガス燃焼式内燃機における燃料ガス供給装置。
1. In a fuel gas supply device that compresses fuel gas and sends it to an internal combustion engine, a bypass pipe connects the vicinity of the internal combustion engine of the compressed fuel gas supply pipe and the compressor suction side, and a bypass pipe connects the compressed fuel gas to the compressed fuel gas before starting the internal combustion engine. a valve that allows flow from the supply pipeline to the bypass pipeline;
A fuel gas supply device for a gas-burning internal combustion engine, characterized in that a condensate separation means is provided in the bypass pipe or a pipe from the bypass pipe branch on the compressor suction side to the compressor. .
JP60060460A 1985-03-25 1985-03-25 Fuel gas feeder for gas internal-combustion engine Granted JPS60216061A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60060460A JPS60216061A (en) 1985-03-25 1985-03-25 Fuel gas feeder for gas internal-combustion engine

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60060460A JPS60216061A (en) 1985-03-25 1985-03-25 Fuel gas feeder for gas internal-combustion engine

Related Parent Applications (1)

Application Number Title Priority Date Filing Date
JP56063073A Division JPS57179356A (en) 1981-04-25 1981-04-25 Fuel gas feeding apparatus for gas combustion type internal combustion engine

Publications (2)

Publication Number Publication Date
JPS60216061A JPS60216061A (en) 1985-10-29
JPH0233869B2 true JPH0233869B2 (en) 1990-07-31

Family

ID=13142897

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60060460A Granted JPS60216061A (en) 1985-03-25 1985-03-25 Fuel gas feeder for gas internal-combustion engine

Country Status (1)

Country Link
JP (1) JPS60216061A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0687483U (en) * 1993-05-31 1994-12-22 株式会社イナックス Deodorant Western style toilet

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7549293B2 (en) * 2006-02-15 2009-06-23 General Electric Company Pressure control method to reduce gas turbine fuel supply pressure requirements
JP5211115B2 (en) * 2010-06-28 2013-06-12 三菱重工業株式会社 Drain device for gas engine charge air cooler
US9371917B2 (en) * 2013-04-30 2016-06-21 General Electric Company Fuel conditioning system
JP2025007356A (en) * 2023-06-30 2025-01-17 カワサキモータース株式会社 Internal combustion engine system and compressor

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0687483U (en) * 1993-05-31 1994-12-22 株式会社イナックス Deodorant Western style toilet

Also Published As

Publication number Publication date
JPS60216061A (en) 1985-10-29

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