JPH0882251A - Liquefied gas fuel supplying device - Google Patents

Liquefied gas fuel supplying device

Info

Publication number
JPH0882251A
JPH0882251A JP6219164A JP21916494A JPH0882251A JP H0882251 A JPH0882251 A JP H0882251A JP 6219164 A JP6219164 A JP 6219164A JP 21916494 A JP21916494 A JP 21916494A JP H0882251 A JPH0882251 A JP H0882251A
Authority
JP
Japan
Prior art keywords
gas
fuel
tank
fuel tank
phase 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
Application number
JP6219164A
Other languages
Japanese (ja)
Inventor
Isao Kikutani
功 菊谷
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.)
Nabco Ltd
Original Assignee
Nabco 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 Nabco Ltd filed Critical Nabco Ltd
Priority to JP6219164A priority Critical patent/JPH0882251A/en
Priority to US08/527,366 priority patent/US5540208A/en
Publication of JPH0882251A publication Critical patent/JPH0882251A/en
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • 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

  • Output Control And Ontrol Of Special Type Engine (AREA)

Abstract

PURPOSE: To realize a liquefied gas fuel supplying device which dispenses with the attachment and detachment of an additional device and can effectively utilize an excessive gas phase gas. CONSTITUTION: This device has a discharge passage 3 for discharging an excessive gas phase gas 1b from a fuel tank 1, a catalytic combusting means 4 provided on the terminal end of the discharge passage 3, a discharge control valve 5 for performing the communication and interruption between the fuel tank 1 and the catalytic combusting means 4, a buffer tank 8 provided between the discharge control valve 5 and a first relief valve through a branched part 7, and a reliquefying device 9 allowed to communicate with the buffer tank 8 to liquefy the excessive gas phase gas 1b. Thus, the excessive gas phase gas 1b is decomposed into carbon dioxide and steam by the catalytic combusting means 4 to prevent air pollution. An additional device for using the excessive gas phase gas 1b in a domestic gas equipment is dispensed with.

Description

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

【0001】[0001]

【産業上の利用分野】この発明は、乗用自動車等に搭載
された内燃機関に天然ガス等の液化ガス燃料を供給する
液化ガス燃料供給装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a liquefied gas fuel supply system for supplying a liquefied gas fuel such as natural gas to an internal combustion engine mounted on a passenger car or the like.

【0002】[0002]

【従来の技術】従来、乗用自動車等の燃料タンクに貯蔵
した液化ガス燃料を気化し、燃料供給路を介して原動機
である内燃機関に供給する液化ガス燃料供給装置があっ
た。この液化ガス燃料供給装置としては、例えば、特開
平4−325757号公報に記載されているように、吸蔵タン
ク内で発生する余剰気相ガスを余剰気相ガス吸蔵タンク
に吸蔵し、更に余剰気相ガスを家庭用ガス器具等の燃料
として再利用することにより、燃料資源の節約及び大気
汚染の防止を図ろうとするものがある。
2. Description of the Related Art Conventionally, there has been a liquefied gas fuel supply device which vaporizes a liquefied gas fuel stored in a fuel tank of a passenger car or the like and supplies it to an internal combustion engine as a prime mover through a fuel supply passage. As the liquefied gas fuel supply device, for example, as described in JP-A-4-325757, the excess gas phase gas generated in the storage tank is stored in the excess gas phase gas storage tank, and the excess gas is further stored. Some of them attempt to save fuel resources and prevent air pollution by reusing the phase gas as fuel for household gas appliances and the like.

【0003】[0003]

【発明が解決しようとする課題】上記例示の液化ガス燃
料供給装置では、余剰気相ガスを家庭用ガス器具等に導
通するための配管類や減圧弁等の付加装置の設置が必要
となり、また車両を運行するときに前記配管類を切離
し、駐車するときに前記配管類を連結しなければなら
ず、不便である。
The liquefied gas fuel supply system illustrated above requires the installation of additional equipment such as piping and pressure reducing valves for conducting excess gas phase gas to household gas appliances. This is inconvenient because the pipes must be disconnected when the vehicle is operating and must be connected when the vehicle is parked.

【0004】この発明の目的は、付加装置の着脱が不要
で且つ余剰気相ガスを有効利用できる液化ガス燃料供給
装置を提供することである。
It is an object of the present invention to provide a liquefied gas fuel supply device which does not require attachment / detachment of an additional device and can effectively utilize surplus gas phase gas.

【0005】[0005]

【課題を解決するための手段】請求項1記載の液化ガス
燃料供給装置は、燃料タンク内に貯蔵された液化ガス燃
料を気化し、燃料供給路に設けたサージタンクを介して
内燃機関へ供給する液化ガス燃料供給装置であって、燃
料タンクから余剰気相ガスを排出する排出路と、該排出
路の終端に設けた触媒燃焼手段と、排出路の途中に設け
られ燃料タンクと触媒燃焼手段を連通・遮断する排出制
御弁と、排出制御弁と燃料タンクの間に分岐部を介して
設けたバッファタンクと、該バッファタンクに連通し余
剰気相ガスを液化して燃料タンクへ供給する再液化装置
とを備えたものである。
A liquefied gas fuel supply apparatus according to claim 1 vaporizes a liquefied gas fuel stored in a fuel tank and supplies it to an internal combustion engine via a surge tank provided in a fuel supply passage. A liquefied gas fuel supply device for discharging excess gas from a fuel tank, a catalyst combustion means provided at the end of the discharge path, and a fuel tank and a catalyst combustion means provided in the middle of the discharge path. An exhaust control valve that connects and disconnects the fuel tank, a buffer tank that is provided between the exhaust control valve and the fuel tank via a branch, and a refueling tank that communicates with the buffer tank to liquefy excess gas gas and supply it to the fuel tank. And a liquefaction device.

【0006】請求項2記載の液化ガス燃料供給装置は、
バッファタンクと再液化装置の間に供給制御弁を設け、
該供給制御弁が、バッファタンク内が所定圧に達したと
きに連通するようにしたものである。
The liquefied gas fuel supply device according to claim 2 is
A supply control valve is provided between the buffer tank and the reliquefaction device,
The supply control valve is adapted to communicate when the inside of the buffer tank reaches a predetermined pressure.

【0007】請求項3記載の液化ガス燃料供給装置は、
排出路の燃料タンクと分岐部の間に、分岐部から燃料タ
ンクへの余剰気相ガスの流入を規制する逆止弁を設け、
サージタンク内が所定圧に達すると、サージタンクと分
岐部を連通するリリーフ弁を設けたものである。
The liquefied gas fuel supply device according to claim 3 is
Between the fuel tank and the branch portion of the discharge passage, a check valve for restricting the inflow of the surplus gas phase gas from the branch portion to the fuel tank is provided,
When the inside of the surge tank reaches a predetermined pressure, a relief valve that connects the surge tank and the branch portion is provided.

【0008】請求項4記載の液化ガス燃料供給装置は、
触媒燃焼手段が、燃焼触媒層と、燃焼触媒層を燃料タン
ク内の余剰気相ガスが所定圧に達したときに加熱する加
熱手段と、燃焼触媒層が所定温度に達したことを検知し
て排出制御弁を連通させる排出制御部とからなるもので
ある。
The liquefied gas fuel supply device according to claim 4 is
The catalytic combustion means detects the combustion catalyst layer, the heating means for heating the combustion catalyst layer when the excess gas phase gas in the fuel tank reaches a predetermined pressure, and the fact that the combustion catalyst layer reaches a predetermined temperature. And a discharge control section for communicating the discharge control valve.

【0009】[0009]

【作用】請求項1記載の液化ガス燃料供給装置による
と、燃料タンク内の余剰気相ガスが所定圧に達すると排
出制御弁が連通状態になり、燃料タンク内の余剰気相ガ
スを排出路を経て排出し、バッファタンクに貯蔵するこ
とができる。更に、バッファタンク内の余剰気相ガスを
再液化装置で液化して燃料タンクに供給できるので、余
剰気相ガスを燃料として再利用することができる。ま
た、余剰気相ガスを、排出路の終端に設けた触媒燃焼手
段で触媒燃焼することにより、二酸化炭素と水蒸気に分
解し大気に放出することができる。
According to the liquefied gas fuel supply device of the first aspect, when the surplus gas phase gas in the fuel tank reaches a predetermined pressure, the discharge control valve is brought into a communication state and the surplus gas phase gas in the fuel tank is discharged. It can be discharged through and stored in a buffer tank. Furthermore, since the excess gas phase gas in the buffer tank can be liquefied by the reliquefaction device and supplied to the fuel tank, the excess gas phase gas can be reused as fuel. Further, the excess gas phase gas can be decomposed into carbon dioxide and water vapor and released into the atmosphere by catalytically burning with the catalytic combustion means provided at the end of the discharge passage.

【0010】請求項2記載の液化ガス燃料供給装置によ
ると、バッファタンク内が所定圧に達したときに、バッ
ファタンクと再液化装置の間に設けた供給制御弁が連通
状態となって、バッファタンク内の余剰気相ガスが再液
化装置へ供給されるように構成しているので、再液化装
置を起動させる頻度を抑え、余剰気相ガスを効率良く再
利用することができる。また、余剰気相ガスが燃料タン
ク内に逆流を防止することができる。
According to the liquefied gas fuel supply device of the second aspect, when the pressure in the buffer tank reaches a predetermined pressure, the supply control valve provided between the buffer tank and the reliquefaction device is in a communication state, and the buffer tank Since the excess gas phase gas in the tank is configured to be supplied to the reliquefaction device, the frequency of activating the reliquefaction device can be suppressed and the excess gas phase gas can be efficiently reused. Further, the excess gas phase gas can be prevented from flowing back into the fuel tank.

【0011】請求項3記載の液化ガス燃料供給装置によ
ると、排出路の分岐部と燃料タンクの間に設けた逆止弁
により、分岐部側から余剰気相ガスが切換弁へ流入する
のを規制しているので、燃料供給路に設けたサージタン
ク内が所定圧に達してリリーフ弁が連通状態になると、
サージタンク内の気相ガス燃料が排出路の分岐部を経て
バッファタンク内に流入する。
According to the liquefied gas fuel supply device of the third aspect, the check valve provided between the branch portion of the discharge passage and the fuel tank prevents the excess gas phase gas from flowing into the switching valve from the branch portion side. Since it is regulated, if the inside of the surge tank provided in the fuel supply path reaches a predetermined pressure and the relief valve is in communication,
Gas-phase gas fuel in the surge tank flows into the buffer tank through the branch portion of the discharge path.

【0012】請求項4記載の液化ガス燃料供給装置によ
ると、燃料タンク内の余剰気相ガスが所定圧に達すると
加熱手段により燃焼触媒層の加熱が開始され、更に燃焼
触媒層が所定温度に達すると排出制御部により排出制御
弁を連通させるので、余剰気相ガスが排出制御弁を経て
触媒燃焼層に供給されるに際して、触媒燃焼層の予熱を
完了しておくことができる。このため、触媒燃焼層にお
て余剰気相ガスを水素及び二酸化炭素に分解する化学反
応を確実に起こすことができ、不完全な触媒燃焼に伴う
一酸化炭素等の有害排出物の発生や未燃焼ガスの大気放
出を防止することができる。
According to the liquefied gas fuel supply device of the fourth aspect, when the surplus vapor phase gas in the fuel tank reaches a predetermined pressure, the heating means starts heating the combustion catalyst layer, and further the combustion catalyst layer reaches a predetermined temperature. When it reaches, the emission control valve communicates with the emission control valve, so that when the excess gas phase gas is supplied to the catalyst combustion layer through the emission control valve, preheating of the catalyst combustion layer can be completed. Therefore, a chemical reaction for decomposing the surplus gas phase gas into hydrogen and carbon dioxide can be surely caused in the catalytic combustion layer, and harmful emissions such as carbon monoxide due to incomplete catalytic combustion and unreacted It is possible to prevent the combustion gas from being released into the atmosphere.

【0013】[0013]

【実施例】この発明の一実施例の液化ガス燃料供給装置
は、図1に示すように、燃料タンク1内に貯蔵された液
化ガス燃料を気化し、燃料供給路2を介して内燃機関
(図示せず)へ燃料噴射弁を経て供給するものであっ
て、前記燃料タンク1から余剰気相ガス1bを排出する
排出路3と、該排出路3の終端に設けた触媒燃焼手段4
と、同図においてECUで表した中央制御手段と、前記
排出路3の途中に設けられ前記中央制御手段の指令信号
に基づいて前記燃料タンク1と前記触媒燃焼手段4を連
通・遮断する排出制御弁5と、前記燃料タンク1と排出
制御弁5の間に設けられ前記燃料タンク1内の余剰気相
ガス1bが所定圧に達すると連通状態となる第1のリリ
ーフ弁6と、前記排出制御弁5と第1のリリーフ弁6の
間に分岐部7を介して設けたバッファタンク8と、該バ
ッファタンク8に連通し余剰気相ガス1bを液化して前
記燃料タンク1へ供給する再液化装置9とを備えたもの
である。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS As shown in FIG. 1, a liquefied gas fuel supply system according to an embodiment of the present invention vaporizes a liquefied gas fuel stored in a fuel tank 1 and, via a fuel supply passage 2, an internal combustion engine ( (Not shown) via a fuel injection valve, a discharge passage 3 for discharging the surplus vapor phase gas 1b from the fuel tank 1, and a catalytic combustion means 4 provided at the end of the discharge passage 3.
And a central control means represented by an ECU in the figure, and a discharge control which is provided in the middle of the discharge path 3 and connects / disconnects the fuel tank 1 and the catalytic combustion means 4 based on a command signal from the central control means. A valve 5; a first relief valve 6 provided between the fuel tank 1 and the discharge control valve 5 and brought into communication with each other when the surplus gas phase gas 1b in the fuel tank 1 reaches a predetermined pressure; A buffer tank 8 provided between the valve 5 and the first relief valve 6 via a branch portion 7, and a reliquefaction for communicating with the buffer tank 8 and liquefying the excess gas phase gas 1b and supplying it to the fuel tank 1. And the device 9.

【0014】前記燃料供給路2には、前記燃料タンク1
内の液相ガス燃料1aを吸引するポンプ2aと、該ポン
プ2aを経て供給される液相ガス燃料1aを水等を媒体
にして熱交換することにより気化する気化器10と、該
気化器10で気化された気化ガス燃料が内燃機関に供給
する燃料として使用可能な所定圧に達すると連通状態と
なる第2のリリーフ弁11と、所定量の気相ガス燃料を
貯蔵するサージタンク12とを設けている。前記燃料タ
ンク1は、この内部の余剰気相ガス1bの圧力を計測す
る第1の圧力計13を設けている。前記第1のリリーフ
弁6は、前記燃料タンク1内を所定圧に保持することに
より、前記燃料タンク1内での余剰気相ガス1bの発生
を抑制するものである。
The fuel tank 1 is provided in the fuel supply passage 2.
A pump 2a for sucking the liquid-phase gas fuel 1a therein, a vaporizer 10 for vaporizing the liquid-phase gas fuel 1a supplied through the pump 2a by exchanging heat with water as a medium, and the vaporizer 10 A second relief valve 11 that is in a communication state when the vaporized gas fuel vaporized in step 1 reaches a predetermined pressure that can be used as fuel to be supplied to the internal combustion engine; and a surge tank 12 that stores a predetermined amount of vapor-phase gas fuel. It is provided. The fuel tank 1 is provided with a first pressure gauge 13 for measuring the pressure of the surplus vapor phase gas 1b therein. The first relief valve 6 keeps the inside of the fuel tank 1 at a predetermined pressure to suppress the generation of the surplus gas phase gas 1b in the fuel tank 1.

【0015】前記バッファタンク8は、余剰気相ガス供
給路14及び該余剰気相ガス供給路14の途中に設けた
供給制御弁15を経て前記再液化装置9に連通してい
る。前記排出制御弁5と分岐部7の間には、前記バッフ
ァタンク8内の余剰気相ガス1bが所定圧に達したこと
を検知して検知信号を中央制御手段へ発信する第2の圧
力計16を設けている。前記供給制御弁15は、前記第
2の圧力計16の検知信号を受けた中央制御手段からの
指令信号に基づいて前記余剰気相ガス供給路14を連通
・遮断するものである。
The buffer tank 8 communicates with the reliquefaction device 9 via a surplus vapor phase gas supply passage 14 and a supply control valve 15 provided on the way of the surplus vapor phase gas supply passage 14. Between the discharge control valve 5 and the branch portion 7, there is provided a second pressure gauge for detecting that the surplus gas phase gas 1b in the buffer tank 8 has reached a predetermined pressure and transmitting a detection signal to the central control means. 16 are provided. The supply control valve 15 connects / disconnects the surplus gas phase gas supply passage 14 based on a command signal from the central control means that receives the detection signal of the second pressure gauge 16.

【0016】前記排出路3の前記第1のリリーフ弁6と
分岐部7の間には、前記前記分岐部7から前記第1のリ
リーフ弁6への余剰気相ガス1bの流入を規制する逆止
弁3aを設け、前記分岐部7には、前記サージタンク1
2内が所定圧に達すると前記燃料供給路2と前記分岐部
7を連通する第3のリリーフ弁17を有する連通路18
を設けている。前記再液化装置9については、周知技術
であるため詳細な説明及び図示を省略するが、例えば、
前記内燃機関を駆動源として前記バッファタンク8内の
余剰気相ガス1bを圧縮する余剰気相ガス圧縮機と、該
余剰気相ガス圧縮機で圧縮された余剰気相ガス1bを冷
却して凝縮させるコールドボックスとから構成されるも
のが挙げられる。この場合、前記コールドボックスとし
ては、冷媒圧縮機,凝縮器,絞り装置及び蒸発器からな
り、窒素ガスを冷媒として冷凍サイクルを形成するもの
が望ましい。
Between the first relief valve 6 and the branch portion 7 of the discharge passage 3, a reverse valve for restricting the inflow of the surplus gas phase gas 1b from the branch portion 7 to the first relief valve 6 is provided. A stop valve 3a is provided, and the surge tank 1 is provided at the branch portion 7.
When the inside of 2 reaches a predetermined pressure, a communication passage 18 having a third relief valve 17 that communicates the fuel supply passage 2 with the branch portion 7
Is provided. Since the reliquefaction device 9 is a well-known technique, detailed description and illustration thereof will be omitted.
A surplus gas phase gas compressor that compresses the surplus gas phase gas 1b in the buffer tank 8 by using the internal combustion engine as a drive source, and cools and condenses the surplus gas phase gas 1b compressed by the surplus gas phase gas compressor. One of them is a cold box to be used. In this case, it is preferable that the cold box includes a refrigerant compressor, a condenser, a throttle device and an evaporator, and forms a refrigeration cycle using nitrogen gas as a refrigerant.

【0017】前記触媒燃焼手段4は、図2に示すよう
に、両側から大気を導入する反応室19の一側面に開口
部19aを設け、該開口部19aに余剰気相ガス1bを
通過可能な多数の貫通孔(図示せず)を設けた燃焼触媒
層20を嵌込み、該燃焼触媒層20に加熱用の電熱線2
1を埋込んだもので、前記排出路3を経て供給される余
剰気相ガス1bを二酸化炭素と加熱水蒸気に分解するも
のである。前記電熱線21の電源としては、例えば自動
車用のバッテリー22が挙げられる。また、前記排出路
3の前記燃焼触媒層20と前記排出制御弁5の間に圧力
補正付き流量制御弁3bを設けてもよい。この場合、前
記燃焼触媒層20における余剰気相ガス1bの反応速度
に応じて前記排出管3から排出する余剰気相ガス1bの
排出量を調節することができる。
As shown in FIG. 2, the catalytic combustion means 4 is provided with an opening 19a on one side surface of a reaction chamber 19 for introducing air from both sides, and an excess gas phase gas 1b can be passed through the opening 19a. A combustion catalyst layer 20 provided with a large number of through holes (not shown) is inserted, and the heating wire 2 for heating is inserted into the combustion catalyst layer 20.
1 in which the excess vapor phase gas 1b supplied through the discharge passage 3 is decomposed into carbon dioxide and heated steam. The power source of the heating wire 21 may be, for example, a battery 22 for an automobile. Further, a flow rate control valve with pressure correction 3b may be provided between the combustion catalyst layer 20 of the discharge passage 3 and the discharge control valve 5. In this case, the discharge amount of the excess gas phase gas 1b discharged from the discharge pipe 3 can be adjusted according to the reaction rate of the excess gas phase gas 1b in the combustion catalyst layer 20.

【0018】なお、前記電熱線21は、所定温度以上に
達しないと触媒燃焼の効率が低い液化天然ガス(LN
G)等が液化ガス燃料として用いられる場合に設置する
のが好ましい。液化ガス燃料として水素ガスを用いる場
合には、もともと温度の高低に関わらず触媒燃焼の効率
が良いので、電熱線21を不用とすることができる。
The heating wire 21 is a liquefied natural gas (LN) having a low catalytic combustion efficiency unless it reaches a predetermined temperature or higher.
It is preferably installed when G) or the like is used as a liquefied gas fuel. When hydrogen gas is used as the liquefied gas fuel, the heating efficiency of the catalytic combustion is high regardless of the temperature, so that the heating wire 21 can be dispensed with.

【0019】また、図3に示すように、前記排出制御弁
5の下流に排出分岐路24及び圧力補正付き流量制御弁
3cを設け、これら排出分岐路24及び圧力補正付き流
量制御弁3c介して余剰気相ガス1bを燃料電池23に
備えた改質手段(図示せず)へ供給し、この余剰気相ガ
ス1bに前記触媒層20で生成された加熱水蒸気を加え
ると共に触媒反応させることにより水素ガスを生成し、
この水素ガスを前記燃料電池23の燃料極に供給すると
共に、前記燃料電池23の空気極に大気を導入すること
により起電力を得るようにしてもよい。この場合、前記
燃料電池23の起電力により前記バッテリー22を充電
できるので、長期間駐車しても前記バッテリー22が自
己放電して内燃機関が始動不能となるのを防止できる。
また、前記燃料電池23としてはリン酸型のものが望ま
しい。
Further, as shown in FIG. 3, a discharge branch passage 24 and a flow control valve 3c with pressure correction are provided downstream of the discharge control valve 5, and the discharge branch passage 24 and the flow control valve 3c with pressure correction are provided. The excess vapor phase gas 1b is supplied to a reforming means (not shown) provided in the fuel cell 23, and the heated vapor generated in the catalyst layer 20 is added to the excess vapor phase gas 1b to cause a catalytic reaction and hydrogen. Produces gas,
Electromotive force may be obtained by supplying this hydrogen gas to the fuel electrode of the fuel cell 23 and introducing the atmosphere into the air electrode of the fuel cell 23. In this case, since the battery 22 can be charged by the electromotive force of the fuel cell 23, it is possible to prevent the internal combustion engine from being unable to start due to the self-discharge of the battery 22 even if the vehicle is parked for a long time.
Further, the fuel cell 23 is preferably a phosphoric acid type.

【0020】以上のように構成した液化ガス燃料供給装
置にれば、内燃機関を運転する際には、前記燃料タンク
1内の液相ガス燃料1aを気化し、前記燃料供給路2を
経て内燃機関に供給される。一方、前記燃料タンク1内
の余剰気相ガス1bの圧力が所定圧に達すると、前記第
1のリリーフ弁6が連通状態となって前記燃料タンク1
内の余剰気相ガス1bか前記バッファタンク8内へ流入
する。また、内燃機関を比較的低回転で運転する等して
燃料消費量が減少し、これによって前記サージタンク内
の圧力が上昇し所定値に達すると、前記第3のリリーフ
弁17が連通状態となり、前記サージタンク12内の気
相ガス燃料が前記連通路18及び前記分岐部7を経て前
記バッファタンク8内に流入する。
According to the liquefied gas fuel supply apparatus configured as described above, when the internal combustion engine is operated, the liquid phase gas fuel 1a in the fuel tank 1 is vaporized and the internal combustion gas is passed through the fuel supply passage 2. Supplied to the institution. On the other hand, when the pressure of the surplus vapor phase gas 1b in the fuel tank 1 reaches a predetermined pressure, the first relief valve 6 is brought into communication with the fuel tank 1
The surplus vapor phase gas 1b therein flows into the buffer tank 8. Further, when the internal combustion engine is operated at a relatively low speed and the fuel consumption decreases, and the pressure in the surge tank rises to reach a predetermined value, the third relief valve 17 enters the communication state. The gas-phase gas fuel in the surge tank 12 flows into the buffer tank 8 through the communication passage 18 and the branch portion 7.

【0021】更に、前記バッファタンク8内が所定圧に
達すると、前記供給制御弁15が連通状態となって、前
記バッファタンク8内の余剰気相ガス1bが前記余剰気
相ガス供給路14を経て前記再液化装置9へ供給される
と共に、前記再液化装置9により液化されて前記燃料タ
ンク1へ供給されるので、余剰気相ガスを燃料として再
利用することが可能となり経済的である。
Further, when the pressure in the buffer tank 8 reaches a predetermined pressure, the supply control valve 15 is brought into a communication state, and the excess gas phase gas 1b in the buffer tank 8 flows through the excess gas phase gas supply passage 14. Since it is supplied to the reliquefaction device 9 via the reliquefaction device 9 and liquefied by the reliquefaction device 9 and supplied to the fuel tank 1, the excess gas phase gas can be reused as fuel, which is economical.

【0022】また、駐車等のために内燃機関を長時間停
止する際には、前記燃料タンク1内の余剰気相ガス1b
の圧力が所定圧に達すると、前記第1のリリーフ弁6が
連通状態となり、燃料タンク1内の余剰気相ガス1bが
前記バッファタンク8へ流入する。更に、前記バッファ
タンク8内が所定圧に達すると、前記排出制御弁5が連
通状態となり、前記バッファタンク8内に貯蔵した余剰
気相ガス1bが前記触媒燃焼手段4に供給され、二酸化
炭素と水蒸気に分解されて大気に放出される。このた
め、大気汚染を伴うことなく余剰気相ガス1bを処理す
ることができ、また従来のように余剰気相ガス1bを家
庭用ガス器具で使用するための付加装置等が不要であ
る。
When the internal combustion engine is stopped for a long time for parking or the like, the surplus gas phase gas 1b in the fuel tank 1 is
When the pressure reaches a predetermined pressure, the first relief valve 6 is brought into a communication state, and the surplus vapor phase gas 1b in the fuel tank 1 flows into the buffer tank 8. Further, when the pressure in the buffer tank 8 reaches a predetermined pressure, the discharge control valve 5 is brought into a communication state, and the excess gas phase gas 1b stored in the buffer tank 8 is supplied to the catalytic combustion means 4 to generate carbon dioxide. It is decomposed into water vapor and released into the atmosphere. Therefore, the surplus vapor phase gas 1b can be treated without causing air pollution, and an additional device or the like for using the surplus vapor phase gas 1b in a household gas appliance unlike the conventional case is unnecessary.

【0023】また、燃料タンク1内の余剰気相ガス1b
が所定圧に達したことを前記第1の圧力計13で検知
し、これに基づいて前記電熱線21を通電状態にする熱
制御手段と、前記燃焼触媒層20が所定温度に達したこ
とを検知して前記排出制御弁5を連通させる排出制御部
とを、前記中央制御手段に組込んだ構成としてもよい。
この場合、前記燃料タンク1内の余剰気相ガス1bが所
定圧に達すると前記加熱手段により前記燃焼触媒層20
の加熱が開始され、更に前記燃焼触媒層20が所定温度
に達すると前記排出制御弁5が連通状態となるので、余
剰気相ガス1bが前記排出制御弁5を経て前記触媒燃焼
層20に供給されるに際して、前記触媒燃焼層20の予
熱を完了しておくことができる。このため、前記触媒燃
焼層20において余剰気相ガス1bを水素及び二酸化炭
素に分解する化学反応を確実に起こすことができ、不完
全な触媒燃焼に伴う一酸化炭素等の有害排出物の発生を
防止することができる。
Further, the surplus gas phase gas 1b in the fuel tank 1
Has reached a predetermined pressure by the first pressure gauge 13, and based on this, heat control means for turning on the heating wire 21 and the fact that the combustion catalyst layer 20 has reached a predetermined temperature. A discharge control unit that detects and communicates the discharge control valve 5 may be incorporated in the central control means.
In this case, when the surplus gas phase gas 1b in the fuel tank 1 reaches a predetermined pressure, the combustion catalyst layer 20 is heated by the heating means.
When the combustion catalyst layer 20 reaches a predetermined temperature and the exhaust control valve 5 is brought into a communication state, the excess gas phase gas 1b is supplied to the catalytic combustion layer 20 through the exhaust control valve 5. At this time, the preheating of the catalyst combustion layer 20 can be completed. Therefore, a chemical reaction for decomposing the surplus gas phase gas 1b into hydrogen and carbon dioxide can be surely caused in the catalytic combustion layer 20, and generation of harmful emissions such as carbon monoxide due to incomplete catalytic combustion. Can be prevented.

【0024】なお、前記燃料タンク3の下部には、液化
ガス燃料を供給する供給口25を設けられており、前記
排出管3の前記燃料タンク1と切換弁10との間には、
前記供給口25から液化ガス燃料を供給する際に、前記
燃料タンク1内に滞留している余剰気相ガス1bを排出
するための排出口26を設けている。
A supply port 25 for supplying liquefied gas fuel is provided in the lower portion of the fuel tank 3, and between the fuel tank 1 of the discharge pipe 3 and the switching valve 10,
When the liquefied gas fuel is supplied from the supply port 25, a discharge port 26 for discharging the excess gas phase gas 1b staying in the fuel tank 1 is provided.

【0025】[0025]

【発明の効果】請求項1記載の液化ガス燃料供給装置に
よると、排出制御弁を連通状態にすると燃料タンク内の
余剰気相ガスを排出路を経て排出すると共にバッファタ
ンクに貯蔵できるので、燃料タンクの爆発事故を防止す
ることができる。更に、バッファタンクに貯蔵した余剰
気相ガスを再液化装置により液化して燃料タンクへ供給
できるので、余剰気相ガスを燃料として再利用し燃料費
の節減を図ることができる。しかも、バッファタンク内
の余剰気相ガスを、排出路の終端に設けた触媒燃焼手段
で触媒燃焼することにより、二酸化炭素と水蒸気に分解
して大気中に放出することもできる。
According to the liquefied gas fuel supply device of the first aspect of the present invention, when the discharge control valve is in the communicating state, the surplus gas phase gas in the fuel tank can be discharged through the discharge passage and stored in the buffer tank. It is possible to prevent the explosion accident of the tank. Furthermore, since the surplus vapor phase gas stored in the buffer tank can be liquefied by the reliquefaction device and supplied to the fuel tank, the surplus vapor phase gas can be reused as fuel to reduce the fuel cost. Moreover, the surplus gas phase gas in the buffer tank can be decomposed into carbon dioxide and water vapor and released into the atmosphere by catalytically burning with the catalytic burning means provided at the end of the discharge passage.

【0026】従って、余剰気相ガスの再利用が可能とな
り経済的であることに加え、大気汚染を伴うことなく余
剰気相ガスを処理し、また従来のように余剰気相ガスを
家庭用ガス器具で燃焼させるための付加装置の着脱が不
要となり、使い勝手が向上する。
Therefore, in addition to being economical because the excess gas phase gas can be reused, the excess gas phase gas is treated without causing air pollution, and the excess gas phase gas is used as a gas for household use as in the conventional case. It is not necessary to attach or detach an additional device for burning with a device, which improves usability.

【0027】請求項2記載の液化ガス燃料供給装置によ
ると、バッファタンク内が所定圧に達したときに、バッ
ファタンクと再液化装置の間に設けた供給制御弁が連通
状態となって、バッファタンク内の余剰気相ガスが再液
化装置へ供給されるように構成しているので、再液化装
置を起動させる頻度を抑え、余剰気相ガスを効率良く再
利用することができる。また、余剰気相ガスが燃料タン
ク内に逆流を防止することができる。このため、燃料タ
ンク内の液相ガスが余剰気相ガスによって加熱されて気
化するのを防止することができる。
According to the liquefied gas fuel supply device of the second aspect, when the pressure in the buffer tank reaches a predetermined pressure, the supply control valve provided between the buffer tank and the reliquefaction device is in a communicating state, and Since the excess gas phase gas in the tank is configured to be supplied to the reliquefaction device, the frequency of activating the reliquefaction device can be suppressed and the excess gas phase gas can be efficiently reused. Further, the excess gas phase gas can be prevented from flowing back into the fuel tank. Therefore, it is possible to prevent the liquid phase gas in the fuel tank from being heated and vaporized by the surplus gas phase gas.

【0028】請求項3記載の液化ガス燃料供給装置によ
ると、サージタンク内が所定圧に達すると排出路とサー
ジタンクをリリーフ弁が連通状態となり、サージタンク
内の気相ガス燃料が排出路へ流入する。このため、例え
ば内燃機関を比較的低回転で運転する等して燃料消費量
が減少しても、燃料供給路に設けたサージタンクが高圧
になるのを防止し、安定した燃料の供給が可能である。
また、排出路に設けた逆止弁により余剰気相ガス又はリ
リーフ弁を経て排出路に流入したサージタンク内の気相
ガス燃料又は排出路内に滞留した余剰気相ガスが燃料タ
ンク内へ逆流するのを防止することができる。
According to the liquefied gas fuel supply device of the third aspect, when the pressure in the surge tank reaches a predetermined pressure, the relief valve connects the discharge passage and the surge tank so that the gas fuel gas in the surge tank is discharged to the discharge passage. Inflow. Therefore, even if the fuel consumption is reduced by operating the internal combustion engine at a relatively low speed, for example, it is possible to prevent the surge tank provided in the fuel supply passage from becoming high in pressure and to supply a stable fuel. Is.
In addition, the check valve provided in the discharge path causes excess gas phase gas or gas phase gas fuel in the surge tank that has flowed into the discharge path through the relief valve or excess gas phase gas accumulated in the discharge path to flow back into the fuel tank. Can be prevented.

【0029】請求項4記載の液化ガス燃料供給装置によ
ると、燃料タンク内の余剰気相ガスが所定圧に達すると
加熱手段により燃焼触媒層の加熱が開始され、更に燃焼
触媒層が所定温度に達すると排出制御部により排出制御
弁を連通させるので、余剰気相ガスが排出制御弁を経て
触媒燃焼層に供給されるに際して、触媒燃焼層の予熱を
完了しておくことができる。このため、触媒燃焼層にお
いて余剰気相ガスを水素及び二酸化炭素に分解する化学
反応を確実に起こすことができ、不完全な触媒燃焼に伴
う一酸化炭素等の有害排出物の発生を防止して、大気汚
染を防止することができる。
According to the liquefied gas fuel supply apparatus of the fourth aspect, when the surplus vapor phase gas in the fuel tank reaches a predetermined pressure, the heating means starts heating the combustion catalyst layer, and further the combustion catalyst layer reaches a predetermined temperature. When it reaches, the emission control valve communicates with the emission control valve, so that when the excess gas phase gas is supplied to the catalyst combustion layer through the emission control valve, preheating of the catalyst combustion layer can be completed. Therefore, a chemical reaction for decomposing the surplus gas phase gas into hydrogen and carbon dioxide can be surely caused in the catalytic combustion layer, and the generation of harmful emissions such as carbon monoxide due to incomplete catalytic combustion is prevented. , Can prevent air pollution.

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

【図1】この発明の一実施例の液化ガス燃料供給装置の
概略図。
FIG. 1 is a schematic diagram of a liquefied gas fuel supply device according to an embodiment of the present invention.

【図2】この発明の一実施例の液化ガス燃料供給装置に
おける触媒燃焼手段の概略図。
FIG. 2 is a schematic diagram of catalytic combustion means in the liquefied gas fuel supply device according to one embodiment of the present invention.

【図3】この発明の一実施例の液化ガス燃料供給装置に
おける触媒燃焼手段の変形例の概略図。
FIG. 3 is a schematic view of a modified example of the catalytic combustion means in the liquefied gas fuel supply device of one embodiment of the present invention.

【符号の説明】[Explanation of symbols]

1 燃料タンク 2 燃料供給路 3 排出路 4 触媒燃焼手段 5 排出制御弁 7 分岐部 8 バッファタンク 9 再液化供給装置 12 サージタンク 1 Fuel Tank 2 Fuel Supply Channel 3 Discharge Channel 4 Catalytic Combustion Means 5 Emission Control Valve 7 Branch Section 8 Buffer Tank 9 Reliquefaction Supply Device 12 Surge Tank

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 燃料タンク内に貯蔵された液化ガス燃料
を気化し、燃料供給路に設けたサージタンクを介して内
燃機関へ供給する液化ガス燃料供給装置であって、前記
燃料タンクから余剰気相ガスを排出する排出路と、該排
出路の終端に設けた触媒燃焼手段と、前記排出路の途中
に設けられ前記燃料タンクと触媒燃焼手段を連通・遮断
する排出制御弁と、前記排出制御弁と燃料タンクの間に
分岐部を介して設けたバッファタンクと、該バッファタ
ンクに連通し前記余剰気相ガスを液化して前記燃料タン
クへ供給する再液化装置とを備えた液化ガス燃料供給装
置。
1. A liquefied gas fuel supply device which vaporizes liquefied gas fuel stored in a fuel tank and supplies it to an internal combustion engine through a surge tank provided in a fuel supply path, wherein excess gas is supplied from the fuel tank. An exhaust passage for exhausting the phase gas, a catalytic combustion means provided at the end of the exhaust passage, an exhaust control valve provided in the middle of the exhaust passage for connecting and disconnecting the fuel tank and the catalytic combustion means, and the exhaust control Liquefied gas fuel supply including a buffer tank provided between a valve and a fuel tank via a branch portion, and a reliquefaction device that communicates with the buffer tank and liquefies the excess gas phase gas to supply the liquefied gas to the fuel tank apparatus.
【請求項2】 前記バッファタンクと前記再液化装置の
間に供給制御弁を設け、該供給制御弁が、前記バッファ
タンク内が所定圧に達したときに連通するようにした請
求項1記載の液化ガス燃料供給装置。
2. A supply control valve is provided between the buffer tank and the reliquefaction device, and the supply control valve is connected when the pressure in the buffer tank reaches a predetermined pressure. Liquefied gas fuel supply device.
【請求項3】 前記排出路の前記燃料タンクと分岐部の
間に、前記分岐部から前記燃料タンクへの余剰気相ガス
の流入を規制する逆止弁を設け、前記サージタンク内が
所定圧に達すると、前記サージタンクと分岐部を連通す
るリリーフ弁を設けた請求項1記載の液化ガス燃料供給
装置。
3. A check valve for restricting an inflow of surplus gas phase gas from the branch portion to the fuel tank is provided between the fuel tank and the branch portion of the discharge passage, and the inside of the surge tank has a predetermined pressure. 2. The liquefied gas fuel supply device according to claim 1, further comprising a relief valve that communicates the surge tank with the branch portion when reaching the temperature.
【請求項4】 前記触媒燃焼手段が、前記燃焼触媒層
と、前記燃焼触媒層を前記燃料タンク内の余剰気相ガス
が所定圧に達したときに加熱する加熱手段と、前記燃焼
触媒層が所定温度に達したことを検知して前記排出制御
弁を連通させる排出制御部とからなる請求項1記載の液
化ガス燃料供給装置。
4. The catalytic combustion means comprises: the combustion catalyst layer; a heating means for heating the combustion catalyst layer when the excess gas phase gas in the fuel tank reaches a predetermined pressure; and the combustion catalyst layer. The liquefied gas fuel supply device according to claim 1, further comprising: an exhaust control unit that detects when a predetermined temperature is reached and connects the exhaust control valve.
JP6219164A 1994-09-13 1994-09-13 Liquefied gas fuel supplying device Pending JPH0882251A (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
JP6219164A JPH0882251A (en) 1994-09-13 1994-09-13 Liquefied gas fuel supplying device
US08/527,366 US5540208A (en) 1994-09-13 1995-09-12 Liquefied gas fuel supply system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6219164A JPH0882251A (en) 1994-09-13 1994-09-13 Liquefied gas fuel supplying device

Publications (1)

Publication Number Publication Date
JPH0882251A true JPH0882251A (en) 1996-03-26

Family

ID=16731210

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6219164A Pending JPH0882251A (en) 1994-09-13 1994-09-13 Liquefied gas fuel supplying device

Country Status (1)

Country Link
JP (1) JPH0882251A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2015127510A (en) * 2013-12-27 2015-07-09 川崎重工業株式会社 Vessel fuel supply system
JP2016037933A (en) * 2014-08-08 2016-03-22 川崎重工業株式会社 Vessel
CN115288894A (en) * 2022-07-26 2022-11-04 江南造船(集团)有限责任公司 Methanol fuel supply system

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2015127510A (en) * 2013-12-27 2015-07-09 川崎重工業株式会社 Vessel fuel supply system
JP2016037933A (en) * 2014-08-08 2016-03-22 川崎重工業株式会社 Vessel
CN115288894A (en) * 2022-07-26 2022-11-04 江南造船(集团)有限责任公司 Methanol fuel supply system
CN115288894B (en) * 2022-07-26 2023-11-07 江南造船(集团)有限责任公司 Methanol fuel supply system

Similar Documents

Publication Publication Date Title
US6916566B2 (en) System and method for rapid preheating of an automotive fuel cell
US5540208A (en) Liquefied gas fuel supply system
JP4542414B2 (en) Hydrogen tank cooling system for hydrogen fuel vehicle
US20110259285A1 (en) Ammonia burning internal combustion engine
AU2019445332B2 (en) Reforming system and engine system
US6591926B2 (en) System and method for recovering energy of a hydrogen gas fuel supply for use in a vehicle
US6716546B2 (en) System and method for supplying air to a fuel cell for use in a vehicle
US6557535B2 (en) System and method for transferring heat from exhaust gasses to compressed gas fuel
CN201003433Y (en) Exhaust gas waste heat utilization device for engine
KR102529370B1 (en) Fuel cell device and automobile with fuel cell device
US8857162B2 (en) Coolant warm-up using exhaust
US6899855B2 (en) Hydrogen-occlusion alloy regenerating apparatus
KR100505472B1 (en) Fuel cell system
JPH0882251A (en) Liquefied gas fuel supplying device
JP5132460B2 (en) Traveling device
JP2002170587A (en) Fuel battery system
JPH0611099A (en) Natural gas supplying device
CN114368336A (en) Refrigerator car with ammonia fuel vaporization cold energy utilization refrigerating system
JP2001213603A (en) Hydrogen supply system for device using hydrogen as fuel
JPH0882252A (en) Liquefied gas fuel supplying device
JP4346055B2 (en) Hydrogen supply system for equipment using hydrogen as fuel
JP2003187836A (en) Hydrogen supply mechanism
JP2000348746A (en) Surplus hydrogen processing method in reform type fuel cell power supply system
JP2001213604A (en) Hydrogen supply system for device using hydrogen as fuel
JP2001268721A (en) Hydrogen supply device for vehicle equipped with fuel cell