JPH02181027A - Hydrogen-or liquefied natural gas-powered engine - Google Patents
Hydrogen-or liquefied natural gas-powered engineInfo
- Publication number
- JPH02181027A JPH02181027A JP33233788A JP33233788A JPH02181027A JP H02181027 A JPH02181027 A JP H02181027A JP 33233788 A JP33233788 A JP 33233788A JP 33233788 A JP33233788 A JP 33233788A JP H02181027 A JPH02181027 A JP H02181027A
- Authority
- JP
- Japan
- Prior art keywords
- oxygen
- suction pump
- enriched air
- natural gas
- liquefied natural
- 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
Landscapes
- Output Control And Ontrol Of Special Type Engine (AREA)
Abstract
Description
【発明の詳細な説明】
[産業上の利用分野]
この発明は水素・液化天然ガス用エンジンに係り、特に
エンジンの負荷運転状態に応じて燃料たる水素と液化天
然ガスとを供給し、これら水素と液化天然ガスとの供給
によって機関性能を向上させる水素・液化天然ガス用エ
ンジンに関する。[Detailed Description of the Invention] [Industrial Application Field] The present invention relates to an engine for hydrogen and liquefied natural gas, and in particular, it supplies hydrogen and liquefied natural gas as fuel according to the load operating state of the engine, and This invention relates to a hydrogen/liquefied natural gas engine that improves engine performance by supplying hydrogen and liquefied natural gas.
[従来の技術]
内燃機関たるエンジンの燃料をしては、主にガソリンや
軽油等が利用されているが、有害排気物質による汚染や
資源の枯渇等の諸問題に鑑み、近時、代替燃料として水
素や液体天然ガス(L N G)が注目されている。こ
れら燃料としての水素や液体天然ガスは、気体燃料であ
ることから空気との混合が良好で均質な混合気を生成す
ることができ、これにより良好な燃焼を得て有害排気物
質の低減を果たすことができる等の種々の利点を有する
ものである。[Conventional technology] Gasoline, diesel oil, etc. are mainly used as fuel for internal combustion engines, but in view of various problems such as pollution caused by harmful exhaust substances and resource depletion, alternative fuels have recently been used. Hydrogen and liquid natural gas (LNG) are attracting attention. Since hydrogen and liquid natural gas are gaseous fuels, they can mix well with air and produce a homogeneous air-fuel mixture, resulting in good combustion and a reduction in harmful exhaust emissions. It has various advantages such as:
このようなエンジンとしては、例えば、特公昭57−4
808号公報や特開昭56−162226号公報、特開
昭58−119928号公報に夫々開示されるものがあ
る。As such an engine, for example, the special public
Some of these are disclosed in Japanese Patent Application Laid-Open No. 808, Japanese Patent Application Laid-Open No. 162226-1980, and Japanese Patent Application Laid-open No. 119928-1987, respectively.
特公昭57−4808号公報には、メタルハイドライド
を加熱して水素を発生させるべく供給される排気ガスの
供給量を、前記発生する水素の圧力によって調整するこ
とにより、水素の安定供給を図った水素エンジンが開示
されている。Japanese Patent Publication No. 57-4808 discloses a method for stably supplying hydrogen by adjusting the amount of exhaust gas supplied to heat metal hydride to generate hydrogen according to the pressure of the generated hydrogen. A hydrogen engine is disclosed.
また、特開昭5Ei−162226号公報には、低圧圧
縮した液化天然ガスを灯油等の溶媒に溶解して貯留し、
この溶媒上に気化して滞留する液化天然ガスを燃料とす
る液化天然ガスエンジンが開示されている。In addition, Japanese Patent Application Laid-Open No. 5Ei-162226 discloses that liquefied natural gas compressed at low pressure is dissolved in a solvent such as kerosene and stored.
A liquefied natural gas engine that uses liquefied natural gas vaporized and retained on this solvent as fuel has been disclosed.
更に、特開昭58−119928号公報には、燃焼室に
2つ設けた吸気弁の両側に夫々排気弁と水素供給弁とを
対向配設することにより、高温の排気弁に向かう水素の
流れを空気の流れにより邪魔して過早着火・ノッキング
の発生を防止した水素エンジンが開示されている。Furthermore, Japanese Patent Application Laid-Open No. 58-119928 discloses that by arranging an exhaust valve and a hydrogen supply valve facing each other on both sides of two intake valves provided in a combustion chamber, hydrogen flows toward the high-temperature exhaust valve. A hydrogen engine has been disclosed in which the occurrence of premature ignition and knocking is prevented by blocking the flow of air.
[発明が解決しようとする問題点]
ところで、従来の水素・液化天然ガス用エンジンにおい
ては、酸素富化空気供給手段の酸素富化膜から高酸素濃
度の空気を得るために、吸気ポンプによって酸素富化膜
の前後部位に所定の圧力差を生じさせている。[Problems to be Solved by the Invention] Incidentally, in conventional hydrogen/liquefied natural gas engines, in order to obtain air with high oxygen concentration from the oxygen enriched membrane of the oxygen enriched air supply means, oxygen is supplied by the intake pump. A predetermined pressure difference is created between the front and rear parts of the enrichment membrane.
そして、吸引ポンプにより圧力差を大とするとともに空
気流量を大とすると、吸引ポンプが高温となり、破損が
生ずる惧れがある。つまり、現行の吸引ポンプの限界使
用可能温度は約120 ’Cてあり、上述の要求酸素濃
度と流量とを満足させるには約80℃の温度上昇がある
ことにより、特に夏場での長時間の高速走行や登板時に
おいて前記吸引ポンプの破損頻度が人となるという不都
合がある。If the suction pump increases the pressure difference and the air flow rate, the suction pump will become hot and there is a risk that it will be damaged. In other words, the maximum usable temperature of current suction pumps is approximately 120'C, and in order to satisfy the above-mentioned required oxygen concentration and flow rate, the temperature must rise by approximately 80'C, so There is an inconvenience that the suction pump is damaged more frequently during high-speed driving or when pitching.
[発明の目的]
そこでこの発明の目的は、」二連不都合を除去するため
に、水素参液化天然ガス用エンジンの酸素富化空気供給
手段の取入り側と取出口側との間に所定の圧力差を生じ
させる吸引ポンプを設けるとともに、酸素富化空気供給
手段の排気口に排気ファンを設け、吸引ポンプを冷却す
べく排気ファンの下流側を吸引ポンプに指向させて設け
たことにより、排気ファンからの排風を吸引ポンプに指
向させ、吸引ポンプを確実に冷却することができ、吸引
ポンプの損傷を防止し得る水素・液化天然ガス用エンジ
ンを実現するにある。[Object of the Invention] Therefore, the object of the present invention is to provide a predetermined gap between the intake side and the outlet side of the oxygen-enriched air supply means of a hydrogen-filled liquefied natural gas engine in order to eliminate the double disadvantage. In addition to providing a suction pump that creates a pressure difference, an exhaust fan is provided at the exhaust port of the oxygen-enriched air supply means, and the downstream side of the exhaust fan is directed toward the suction pump to cool the suction pump. To provide a hydrogen/liquefied natural gas engine that can reliably cool the suction pump by directing exhaust air from a fan toward the suction pump, and can prevent damage to the suction pump.
口問題点を解決するための手段]
この目的を達成するためにこの発明は、エンジンの負荷
運転状態に応じて燃料たる水素と液化天然ガスとのいず
れか一方を供給する水素O液化天然ガス用エンジンにお
いて、酸素富化空気供給手段の取入口側と取出口側との
間に所定の圧力差を生じさせる吸引ポンプを設けるとと
もに前記酸素富化空気供給手段の排気口に排気ファンを
設け、前記吸引ポンプを冷却すべく前記排気ファンの下
流側を前記吸引ポンプに指向させて設けたことを特徴と
する。[Means for Solving the Problem] To achieve this object, the present invention provides a hydrogen O liquefied natural gas fuel supply system that supplies either hydrogen as a fuel or liquefied natural gas depending on the load operating state of the engine. In the engine, a suction pump is provided to create a predetermined pressure difference between the intake side and the outlet side of the oxygen-enriched air supply means, and an exhaust fan is provided at the exhaust port of the oxygen-enriched air supply means, and the In order to cool the suction pump, the downstream side of the exhaust fan is directed toward the suction pump.
[作用]
上述の如く構成したことにより、水素・液化天然ガス用
エンジンを駆動させた際に、排気ファンからの排風を吸
引ポンプに指向させ、吸引ポンプを確実に冷却し、吸引
ポンプの損傷を防止している。[Function] With the above configuration, when the hydrogen/liquefied natural gas engine is driven, the exhaust air from the exhaust fan is directed toward the suction pump, thereby reliably cooling the suction pump and preventing damage to the suction pump. is prevented.
[実施例]
以下図面に基づいてこの発明の実施例を詳細に説明する
。[Examples] Examples of the present invention will be described in detail below based on the drawings.
第1〜3図はこの発明の実施例を示すものである。第1
図において、2は水素・液化天然ガス用エンジン(以下
、 「エンジン」という)、4は酸素富化空気供給手段
たる酸素富化空気供給機構である。この実施例において
、エンジン2は、酸素富化空気を供給されるとともに、
燃料として水素と液化天然ガスとを供給される。1 to 3 show embodiments of this invention. 1st
In the figure, 2 is a hydrogen/liquefied natural gas engine (hereinafter referred to as the "engine"), and 4 is an oxygen-enriched air supply mechanism that is an oxygen-enriched air supply means. In this example, the engine 2 is supplied with oxygen-enriched air and
Hydrogen and liquefied natural gas are supplied as fuel.
前記エンジン2に酸素富化空気を供給する酸素富化空気
供給機構4は、本体6内に特定の気体を選択的に透過さ
せる気体選択性透過膜等の酸素富化空気生成体たる例え
ば酸素富化膜8を備えている。前記本体6の空気の取入
口6a側にはエアクリーナ10を設け、本体6の取出口
6b側には例えば前記エンジン2の駆動力等により駆動
される吸引ポンプ12を設けている。この吸引ポンプ1
2により酸素富化膜8の前記取入口6a側と取出口6b
側との間に圧力差を生じさせ、取出口6b側に酸素富化
膜8により空気中の酸素濃度を高めて酸素富化空気を生
成する。The oxygen-enriched air supply mechanism 4 supplies oxygen-enriched air to the engine 2. A chemical film 8 is provided. An air cleaner 10 is provided on the air intake port 6a side of the main body 6, and a suction pump 12 driven by, for example, the driving force of the engine 2 is provided on the air intake port 6b side of the main body 6. This suction pump 1
2, the intake port 6a side and the outlet port 6b of the oxygen enrichment membrane 8
A pressure difference is generated between the two sides, and the oxygen concentration in the air is increased by the oxygen-enriching membrane 8 on the outlet 6b side to generate oxygen-enriched air.
このように、取出口6b側に空気中の酸素濃度を高めて
酸素富化空気を生成する一方で、取入口6a側には酸素
濃度の低減により窒素濃度の高められた空気として窒素
富化空気が残留生成されることになる。この窒素富化空
気が前記取入ロ6a周辺に滞留すると、取り入れた空気
が窒素富化空気で飽和して酸素富化空気の生成が困難に
なる。In this way, oxygen-enriched air is generated by increasing the oxygen concentration in the air on the intake port 6b side, while nitrogen-enriched air is generated on the intake port 6a side as air with increased nitrogen concentration due to a reduction in oxygen concentration. will be residually generated. If this nitrogen-enriched air stays around the intake hole 6a, the introduced air will become saturated with nitrogen-enriched air, making it difficult to generate oxygen-enriched air.
そこで、前記酸素富化空気供給機構4の本体6に排気口
14を設け、この排気口14に排気ファン16を設ける
とともに、排気口14の下流側142を前記吸引ポンプ
12に指向させて設けている。Therefore, an exhaust port 14 is provided in the main body 6 of the oxygen-enriched air supply mechanism 4, an exhaust fan 16 is provided in the exhaust port 14, and the downstream side 142 of the exhaust port 14 is directed toward the suction pump 12. There is.
これにより、不要な窒素富化空気を外部に排気し得ると
ともに、冷却風としても利用することができる。Thereby, unnecessary nitrogen-enriched air can be exhausted to the outside and can also be used as cooling air.
前記酸素富化膜8の取出口6b側に生成された酸素富化
空気は、前記吸引ポンプ12下流に始端する連通路18
によって、前記エンジン2の吸気通路20始端側に設け
た酸素富化空気の導入室22に供給される。導入室22
内には、後述のベーパライザ66が設けられており、燃
料たる液化天然ガスの気化潜熱により酸素富化空気を冷
却する。The oxygen-enriched air generated on the side of the outlet 6b of the oxygen-enriched membrane 8 flows through a communication path 18 starting downstream of the suction pump 12.
As a result, the oxygen-enriched air is supplied to an oxygen-enriched air introduction chamber 22 provided at the starting end side of the intake passage 20 of the engine 2. Introduction room 22
A vaporizer 66, which will be described later, is provided inside, and cools the oxygen-enriched air using the latent heat of vaporization of liquefied natural gas, which is the fuel.
導入室22で冷却された酸素富化空気は、ミキサ24に
より燃料と混合して混合気を生成し、吸気絞り弁26に
より流量を調整し、吸気弁28を介して燃焼室30に供
給される。燃焼室30で燃焼生成された排気は、排気弁
32を介して排気通路34に排出され外部に排出される
。The oxygen-enriched air cooled in the introduction chamber 22 is mixed with fuel by a mixer 24 to produce an air-fuel mixture, the flow rate is adjusted by an intake throttle valve 26, and the air is supplied to the combustion chamber 30 via an intake valve 28. . Exhaust gas produced by combustion in the combustion chamber 30 is discharged to the exhaust passage 34 via the exhaust valve 32 and exhausted to the outside.
前記酸素富化空気供給機構4の本体6内の酸素富化膜8
は、基準となる基準酸素富化膜8−0と、この基準酸素
富化膜8−0と同様に構成された第1、第2酸素富化膜
8−L 8−2とからなる。Oxygen enrichment membrane 8 in the main body 6 of the oxygen enriched air supply mechanism 4
consists of a reference oxygen enrichment film 8-0 serving as a reference, and first and second oxygen enrichment films 8-L 8-2 configured similarly to this reference oxygen enrichment film 8-0.
これら基準酸素富化膜8−0および第1、第2酸素富化
膜8−1.8−2は、前記取入口6a側に夫々連通する
とともに、取出口6b側に夫々連通している。前記第1
、第2酸素富化膜8−1.8−2の取出口6b側には、
夫々第1、第2制御弁36−1.36−2を設ける。こ
れら第1、第2制御井36−1.36−2は、図示しな
い制御手段に接続している。この制御手段によって第1
、第2制御弁36−1.36−2を開閉することにより
第1、第2酸素富化膜8−1.8−2は取出口6b側に
対して連通・遮断される。The reference oxygen enrichment membrane 8-0 and the first and second oxygen enrichment membranes 8-1, 8-2 communicate with the intake port 6a, respectively, and communicate with the outlet 6b, respectively. Said first
, on the outlet port 6b side of the second oxygen enrichment membrane 8-1.8-2,
First and second control valves 36-1 and 36-2 are provided, respectively. These first and second control wells 36-1 and 36-2 are connected to a control means (not shown). By this control means, the first
By opening and closing the second control valve 36-1.36-2, the first and second oxygen enrichment membranes 8-1.8-2 are communicated with and cut off from the outlet 6b side.
前記本体6の取入口6a側と取出口6b側とには取入口
側圧力センサ38と取出口側圧力センサ40とを設ける
とともに、前記導入室22には導入室圧力センサ42と
導入室吸気温センサ44とを設ける。これら各センサ3
8〜44は、図示しない前記制御手段に接続され、この
制御手段によって、前記取入口側圧力センサ38と取出
口側圧力センサ40とにより夫々検出される圧力の差が
所定圧力となるように、前記吸引ポンプ12を駆動制御
する。An inlet side pressure sensor 38 and an outlet side pressure sensor 40 are provided on the intake port 6a side and the outlet port 6b side of the main body 6, and an introduction chamber pressure sensor 42 and an introduction chamber intake temperature sensor are provided in the introduction chamber 22. A sensor 44 is provided. Each of these sensors 3
8 to 44 are connected to the control means (not shown) so that the difference between the pressures respectively detected by the intake side pressure sensor 38 and the outlet side pressure sensor 40 becomes a predetermined pressure. The suction pump 12 is driven and controlled.
また、導入室22内の圧力は、前記エンジン2の要求す
る酸素富化空気要求量と前記酸素富化空気供給機構4の
供給する酸素富化空気供給量との圧力差になる。そこで
、導入室吸気温センサ44の検出する導入室吸気温を加
味しつつ導入室圧力センサ42の検出する導入室22内
の圧力に応じ、前記制御手段により前記第1、第2制御
弁36−1.36−2を開閉制御して第1、第2酸素富
化膜8−L 8−2を取出口6b側に選択的に連通さ
せることにより、酸素富化膜8の酸素富化空気生成面積
を増減制御する。これにより、酸素濃度の大幅な変動を
招くことなく、エンジン2の酸素富化空気要求量に応じ
て酸素富化空気供給機構4より供給される酸素富化空気
供給量を増減し、適正に供給することができる。Further, the pressure within the introduction chamber 22 is a pressure difference between the amount of oxygen-enriched air required by the engine 2 and the amount of oxygen-enriched air supplied by the oxygen-enriched air supply mechanism 4. Therefore, in accordance with the pressure inside the introduction chamber 22 detected by the introduction chamber pressure sensor 42 while taking into account the introduction chamber intake temperature detected by the introduction chamber intake temperature sensor 44, the control means controls the first and second control valves 36- 1. Generation of oxygen-enriched air in the oxygen-enriched membrane 8 by controlling the opening and closing of 36-2 to selectively connect the first and second oxygen-enriched membranes 8-L 8-2 to the outlet 6b side. Control the increase/decrease in area. As a result, the amount of oxygen-enriched air supplied from the oxygen-enriched air supply mechanism 4 can be increased or decreased according to the amount of oxygen-enriched air required by the engine 2, and the oxygen-enriched air can be supplied appropriately without causing a large change in oxygen concentration. can do.
この酸素富化空気供給機構4の酸素富化空気は、所望に
応じてエンジン2に供給される。つまり、エンジン2の
低負荷運転状態から高負荷運転状態までの全域において
供給することも可能であり、また、特定の負荷運転状態
においてのみ供給することも可能である。なお、符号4
6は導入室22に大気を吸入する吸入用逆止弁、48は
導入室22から大気に排出する排出用逆止弁である。The oxygen-enriched air from the oxygen-enriched air supply mechanism 4 is supplied to the engine 2 as desired. In other words, it is possible to supply the fuel over the entire range from the low-load operating state to the high-load operating state of the engine 2, or it is also possible to supply only in a specific load operating state. In addition, code 4
Reference numeral 6 represents an intake check valve that sucks the atmosphere into the introduction chamber 22, and 48 represents an exhaust check valve that exhausts air from the introduction chamber 22 to the atmosphere.
前記エンジン2に供給される燃料たる水素を貯留する図
示しない水素タンクは、例えば水素化金属(METAL
HYDRIDE)により水素を貯留し、前記ミキサ
24により水素の混合気を生成し、吸気絞り弁26によ
り流量を調整して燃焼室30に供給する。A hydrogen tank (not shown) that stores hydrogen, which is the fuel supplied to the engine 2, is made of, for example, metal hydride (METAL).
HYDRIDE), hydrogen is stored by the mixer 24, a hydrogen mixture is generated by the intake throttle valve 26, and the flow rate is adjusted by the intake throttle valve 26 and supplied to the combustion chamber 30.
また、図示しない水素タンクの加熱機構は、前記エンジ
ン2の冷却水通路50に連絡され、排気ガスの熱により
前記加熱機構に向かって流れる冷却水を昇温させる。Further, a hydrogen tank heating mechanism (not shown) is connected to the cooling water passage 50 of the engine 2, and uses the heat of the exhaust gas to raise the temperature of the cooling water flowing toward the heating mechanism.
前記エンジン2に供給される燃料たる液化天然ガスを貯
留する液化天然ガスタンク52は、液化天然ガス充填管
54により液化天然ガス充填弁5θを介して極低温の液
化した液化天然ガスを充填させる。液化天然ガスタンク
52の液化天然ガスは、液化天然ガス取出弁58により
取出され、液化天然ガス供給管60により供給される。The liquefied natural gas tank 52 that stores liquefied natural gas as fuel to be supplied to the engine 2 is filled with cryogenic liquefied liquefied natural gas through a liquefied natural gas filling pipe 54 and a liquefied natural gas filling valve 5θ. The liquefied natural gas in the liquefied natural gas tank 52 is taken out by the liquefied natural gas take-off valve 58 and supplied by the liquefied natural gas supply pipe 60.
液化天然ガス供給管60には、フィルタ62、電磁弁6
4、ベーパライザ66が順次配設されている。The liquefied natural gas supply pipe 60 includes a filter 62 and a solenoid valve 6.
4. Vaporizers 66 are sequentially arranged.
前記電磁弁64は、図示しない制御手段に接続されてい
る。また、前記ベーパライザ66は、前記導入室22内
に設けられ、酸素富化空気との熱交換により液化天然ガ
スを加温して蒸発させるとともに、酸素富化空気を冷却
する。The solenoid valve 64 is connected to a control means (not shown). Further, the vaporizer 66 is provided in the introduction chamber 22, and heats and evaporates the liquefied natural gas through heat exchange with the oxygen-enriched air, and cools the oxygen-enriched air.
前記ベーパライザ66下流側の液化天然ガス供給管60
は、供給管68に接続され、この供給管68途中にはレ
ギュレータ70が設けられている。Liquefied natural gas supply pipe 60 downstream of the vaporizer 66
is connected to a supply pipe 68, and a regulator 70 is provided in the middle of this supply pipe 68.
供給管68は液化天然ガスをミキサ24に供給し、この
ミキサ24により液化天然ガスの混合気を生成し、吸気
絞り弁26により流量を調整して燃焼室30に供給する
。The supply pipe 68 supplies liquefied natural gas to the mixer 24 , the mixer 24 generates a mixture of liquefied natural gas, the flow rate is adjusted by the intake throttle valve 26 , and the mixture is supplied to the combustion chamber 30 .
また、前記ベーパライザ66は、第2.3図に示す如く
、酸素富化空気を通過させる第1通路72と、この第1
通路72途中に設けた放射状フィン74と、放射状フィ
ン74の中心を通る液化天然ガス(LNG)用第2通路
76とを有する。The vaporizer 66 also includes a first passage 72 through which oxygen-enriched air passes, and a first passage 72, as shown in FIG. 2.3.
It has radial fins 74 provided in the middle of the passage 72, and a second passage 76 for liquefied natural gas (LNG) passing through the center of the radial fins 74.
前記第1通路72下部に熱交換によって結露した酸素富
化空気中の水を収集する収集凹部78を設け、第1〜3
図に示す如く、この収集凹部78下部を始端とし前記排
気口14の下流側14zに終端する水通路80を設ける
。A collection recess 78 is provided at the bottom of the first passage 72 to collect water in the oxygen-enriched air condensed by heat exchange, and the first to third passages
As shown in the figure, a water passage 80 is provided that starts at the lower part of the collection recess 78 and terminates on the downstream side 14z of the exhaust port 14.
次に作用について説明する。Next, the effect will be explained.
前記エンジン2を駆動すると、図示しない制御手段は、
酸素富化空気供給機構4の本体6の取入口6a側の圧力
と取出口6b側の圧力とが所定圧力となるように吸引ポ
ンプ12を駆動制御する。When the engine 2 is driven, the control means (not shown)
The suction pump 12 is driven and controlled so that the pressure on the intake port 6a side and the pressure on the outlet port 6b side of the main body 6 of the oxygen-enriched air supply mechanism 4 become predetermined pressures.
また、導入室22内の圧力に応じて第1、第2制御弁3
6−1.36−2を開閉制御し、第1、第2酸素富化膜
8−L 8−2を取出口6b側に選択的に連通させて
酸素富化膜8の酸素富化空気生成面積を増減制御する。In addition, the first and second control valves 3
6-1.36-2 is controlled to open and close, and the first and second oxygen enrichment membranes 8-L 8-2 are selectively communicated with the outlet 6b to generate oxygen-enriched air in the oxygen enrichment membrane 8. Control the increase/decrease in area.
これにより、酸素濃度の大幅な変動を招くことなく、エ
ンジン2の酸素富化空気要求量に応じて酸素富化空気供
給機構4より供給される酸素富化空気供給量を増減し、
適正に供給する。As a result, the amount of oxygen-enriched air supplied from the oxygen-enriched air supply mechanism 4 can be increased or decreased according to the amount of oxygen-enriched air required by the engine 2 without causing a significant change in oxygen concentration.
Supply appropriately.
このエンジン2の負荷運転状態、例えば、アイドリング
運転状態あるいは低速運転状態の低負荷運転状態や、加
速運転状態あるいは高速運転状態の高負荷運転状態に応
じて水素と液化天然ガスとのいずれか一方供給するよう
に制御する。Either hydrogen or liquefied natural gas is supplied depending on the load operating state of the engine 2, for example, a low-load operating state such as an idling operating state or a low-speed operating state, or a high-load operating state such as an accelerating operating state or a high-speed operating state. control to do so.
また、前記排気ファン16からの排気は、排気口14の
下流側14zから吸引ポンプ12に向けて排出される。Further, the exhaust air from the exhaust fan 16 is discharged toward the suction pump 12 from the downstream side 14z of the exhaust port 14.
そしてこのとき、前記ベーパライザ66内における熱交
換によって結露した水が収集四部78に収集され、水通
路80によって排気口14の下流側14zに案内され、
上述の排気によって前記吸引ポンプ12に吹き付けられ
る。At this time, water condensed by heat exchange within the vaporizer 66 is collected in the collection section 78 and guided to the downstream side 14z of the exhaust port 14 by the water passage 80,
The suction pump 12 is blown by the above-mentioned exhaust gas.
これにより、前記排気ファン16によって排出される排
気で吸引ポンプ12を冷却することができるとともに、
この排気と前記ベーパライザ66からの水とによって水
が吸引ポンプ12に吹き付けられ、水の蒸発熱により吸
引ポンプ12を一層冷却させることができ、実用上有利
である。Thereby, the suction pump 12 can be cooled by the exhaust gas discharged by the exhaust fan 16, and
Water is blown onto the suction pump 12 by this exhaust air and the water from the vaporizer 66, and the suction pump 12 can be further cooled by the heat of evaporation of the water, which is advantageous in practice.
また、前記吸引ポンプ12を確実に冷却できることによ
り、特に夏場での長時間の高速走行や登板時においても
、前記吸引ポンプ12の破損を防止することができるも
のである。Furthermore, since the suction pump 12 can be reliably cooled, it is possible to prevent the suction pump 12 from being damaged, especially when driving at high speed for a long time in the summer or when riding uphill.
更に、前記排気口14の延長と水通路80との形成のみ
で実現できることにより、構成が極端に複雑化せず、コ
ストを低摩に維持でき、経済的に有利である。Furthermore, since this can be achieved by simply extending the exhaust port 14 and forming the water passage 80, the structure is not extremely complicated and costs can be kept low, which is economically advantageous.
[発明の効果コ
以上詳細に説明した如くこの発明によれば、水素・液化
天然ガス用エンジンの酸素富化空気供給手段の取入口側
と取出口側との間に所定の圧力差を生じさせる吸引ポン
プを設けるとともに、酸素=13−
富化空気供給手段の排気口に排気ファンを設け、吸引ポ
ンプを冷却すべく排気ファンの下流側を吸引ポンプに指
向させて設けたので、排気ファンによって排出される排
気で吸引ポンプを確実に冷却することができ、特に夏場
での長時間の高速走行や登板時においても、前記吸引ポ
ンプの破損を防止し得るものである。また、前記酸素富
化空気供給手段の構成が極端に複雑化しないことにより
、コストを低床に維持し得て、経済的に有利である。[Effects of the Invention] As explained in detail above, according to the present invention, a predetermined pressure difference is created between the intake side and the outlet side of the oxygen-enriched air supply means of a hydrogen/liquefied natural gas engine. In addition to providing a suction pump, an exhaust fan was provided at the exhaust port of the oxygen enriched air supply means, and the downstream side of the exhaust fan was directed toward the suction pump in order to cool the suction pump. The suction pump can be reliably cooled by the exhausted air, and damage to the suction pump can be prevented, especially during long hours of high-speed driving or pitching in the summer. Furthermore, since the configuration of the oxygen-enriched air supply means is not extremely complicated, costs can be kept low, which is economically advantageous.
第1〜3図はこの発明の実施例を示し、第1図は水素・
液化天然ガス用エンジンの概略構成図、第2図はベーパ
ライザの概略拡大断面図、第3図は第2図の■−■線に
よるベーパライザの概略端面図である。
図において、2は水素・液化天然ガス用エンジン、4は
酸素富化空気供給機構、6は本体、6aは取入口、6b
は取出口、8は酸素富化膜、10はエアクリーナ、12
は吸引ポンプ、14は排気口、14zは下流側、16は
排気ファン、22は導入室、36−1は第1制御弁、3
6−2は第2制御弁、38は取入口側圧力センサ、40
は取出口側圧力センサ、42は導入室圧力センサ、44
は導入室吸気温センサ、46は吸入用逆止弁、48は排
出用逆止弁、52は液化天然ガスタンク、66はベーパ
ライザ、72は第1通路、74は放射状フィン、76は
第2通路、78は収集凹部、80は水通路である。
特 許 出願人
代 理 人 弁理士
鈴木自動車工業株式会社
西 郷 義 美
第3図1 to 3 show examples of the present invention, and FIG.
FIG. 2 is a schematic enlarged cross-sectional view of a vaporizer, and FIG. 3 is a schematic end view of the vaporizer taken along the line ■-■ in FIG. 2. In the figure, 2 is a hydrogen/liquefied natural gas engine, 4 is an oxygen-enriched air supply mechanism, 6 is the main body, 6a is an intake port, and 6b
is an outlet, 8 is an oxygen enrichment membrane, 10 is an air cleaner, 12
14 is a suction pump, 14 is an exhaust port, 14z is a downstream side, 16 is an exhaust fan, 22 is an introduction chamber, 36-1 is a first control valve, 3
6-2 is a second control valve, 38 is an intake side pressure sensor, 40
is an outlet side pressure sensor, 42 is an inlet chamber pressure sensor, 44
is an inlet room intake temperature sensor, 46 is an intake check valve, 48 is a discharge check valve, 52 is a liquefied natural gas tank, 66 is a vaporizer, 72 is a first passage, 74 is a radial fin, 76 is a second passage, 78 is a collection recess, and 80 is a water passage. Patent Applicant Representative Patent Attorney Yoshimi Saigo Suzuki Automobile Industry Co., Ltd. Figure 3
Claims (1)
化天然ガスとのいずれか一方を供給する水素・液化天然
ガス用エンジンにおいて、酸素富化空気供給手段の取入
口側と取出口側との間に所定の圧力差を生じさせる吸引
ポンプを設けるとともに前記酸素富化空気供給手段の排
気口に排気ファンを設け、前記吸引ポンプを冷却すべく
前記排気ファンの下流側を前記吸引ポンプに指向させて
設けたことを特徴とする水素・液化天然ガス用エンジン
。1. In a hydrogen/liquefied natural gas engine that supplies either hydrogen or liquefied natural gas as a fuel depending on the load operating state of the engine, the connection between the intake side and the outlet side of the oxygen-enriched air supply means A suction pump that generates a predetermined pressure difference between them is provided, and an exhaust fan is provided at the exhaust port of the oxygen-enriched air supply means, and a downstream side of the exhaust fan is directed toward the suction pump in order to cool the suction pump. A hydrogen/liquefied natural gas engine characterized by being equipped with a
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP33233788A JPH02181027A (en) | 1988-12-29 | 1988-12-29 | Hydrogen-or liquefied natural gas-powered engine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP33233788A JPH02181027A (en) | 1988-12-29 | 1988-12-29 | Hydrogen-or liquefied natural gas-powered engine |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH02181027A true JPH02181027A (en) | 1990-07-13 |
Family
ID=18253836
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP33233788A Pending JPH02181027A (en) | 1988-12-29 | 1988-12-29 | Hydrogen-or liquefied natural gas-powered engine |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH02181027A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2010025051A (en) * | 2008-07-23 | 2010-02-04 | Masashi Sato | Power generation device and traveling device |
-
1988
- 1988-12-29 JP JP33233788A patent/JPH02181027A/en active Pending
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2010025051A (en) * | 2008-07-23 | 2010-02-04 | Masashi Sato | Power generation device and traveling device |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US3844262A (en) | Vaporization of exhaust products in hydrogen-oxygen engine | |
| US3862624A (en) | Oxygen-hydrogen fuel use for combustion engines | |
| US4068637A (en) | Multicylinder internal combustion engine | |
| EP0510585B1 (en) | Gas engine | |
| JPH0152655B2 (en) | ||
| JPH02181027A (en) | Hydrogen-or liquefied natural gas-powered engine | |
| CN115977794A (en) | Charge air cooling system for a reciprocating piston internal combustion engine and internal combustion engine | |
| JP2570658B2 (en) | Hydrogen / liquefied natural gas engine | |
| JPH04228827A (en) | Device to reduce atmospheric contamination by internal combustion engine | |
| JP2002188519A (en) | Gas fuel supply system for internal combustion engine | |
| JPS6014894B2 (en) | Secondary air supply control device for exhaust gas purification of internal combustion engines | |
| JPS5827867A (en) | Intake apparatus for internal combustion engine | |
| JP2580546B2 (en) | LNG engine frost prevention device | |
| JPH06264821A (en) | Fuel supply system for CNG engine | |
| JP2570671B2 (en) | LNG engine intake cooling system | |
| JP2622784B2 (en) | Fuel vaporization promotion device for air-cooled gas engine | |
| JP3955142B2 (en) | Evaporative purge control method for internal combustion engine | |
| JP3074228B2 (en) | Gas fuel engine with supercharger | |
| JPH02201068A (en) | Oxygen supplied engine | |
| JP2501562Y2 (en) | Intake cooling structure of LNG engine | |
| JPS58117345A (en) | Fuel-air mixture control device of reformed alcohol gas engine | |
| JPH03145559A (en) | Alcohol reforming engine | |
| JP2889973B2 (en) | Multi-cylinder sub-chamber lean-burn gas engine | |
| JP4378666B2 (en) | Engine liquefied gas supply device | |
| JP3265060B2 (en) | Mixture forming device for gaseous fuel engine |