JPS5937267A - Quick evaporation device for liquid fuel - Google Patents
Quick evaporation device for liquid fuelInfo
- Publication number
- JPS5937267A JPS5937267A JP57146581A JP14658182A JPS5937267A JP S5937267 A JPS5937267 A JP S5937267A JP 57146581 A JP57146581 A JP 57146581A JP 14658182 A JP14658182 A JP 14658182A JP S5937267 A JPS5937267 A JP S5937267A
- Authority
- JP
- Japan
- Prior art keywords
- fuel
- engine
- air
- hot surface
- mixture
- 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
- 239000000446 fuel Substances 0.000 title claims abstract description 58
- 238000001704 evaporation Methods 0.000 title claims abstract description 14
- 230000008020 evaporation Effects 0.000 title claims description 11
- 239000007788 liquid Substances 0.000 title claims description 8
- 238000002347 injection Methods 0.000 claims abstract description 34
- 239000007924 injection Substances 0.000 claims abstract description 34
- 239000000203 mixture Substances 0.000 claims abstract description 20
- 238000010438 heat treatment Methods 0.000 claims abstract description 6
- 239000002245 particle Substances 0.000 claims description 13
- 230000006835 compression Effects 0.000 claims description 4
- 238000007906 compression Methods 0.000 claims description 4
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 abstract description 48
- 239000003502 gasoline Substances 0.000 abstract description 7
- 238000002156 mixing Methods 0.000 abstract description 7
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 abstract description 5
- 238000000034 method Methods 0.000 abstract description 2
- 238000010792 warming Methods 0.000 abstract description 2
- 239000003595 mist Substances 0.000 abstract 1
- 239000007789 gas Substances 0.000 description 13
- 230000001105 regulatory effect Effects 0.000 description 7
- 238000002485 combustion reaction Methods 0.000 description 4
- 230000007423 decrease Effects 0.000 description 3
- 238000009834 vaporization Methods 0.000 description 3
- 230000008016 vaporization Effects 0.000 description 3
- 239000000498 cooling water Substances 0.000 description 2
- 239000002828 fuel tank Substances 0.000 description 2
- 239000000919 ceramic Substances 0.000 description 1
- 230000001276 controlling effect Effects 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 239000002737 fuel gas Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 238000011144 upstream manufacturing Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F02—COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
- F02M—SUPPLYING COMBUSTION ENGINES IN GENERAL WITH COMBUSTIBLE MIXTURES OR CONSTITUENTS THEREOF
- F02M31/00—Apparatus for thermally treating combustion-air, fuel, or fuel-air mixture
- F02M31/02—Apparatus for thermally treating combustion-air, fuel, or fuel-air mixture for heating
- F02M31/16—Other apparatus for heating fuel
- F02M31/18—Other apparatus for heating fuel to vaporise fuel
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02T—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
- Y02T10/00—Road transport of goods or passengers
- Y02T10/10—Internal combustion engine [ICE] based vehicles
- Y02T10/12—Improving ICE efficiencies
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Output Control And Ontrol Of Special Type Engine (AREA)
Abstract
Description
【発明の詳細な説明】
本発明は液体燃料から着火性の良い混合気を形成して内
燃機関に供給し、内燃機関の冷間始動から定常運転まで
を単一燃料の一系統で行うことができるようにした内燃
機関の液体燃料の急速蒸発装置に関し、特にアルコール
燃料の急速蒸発装置に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention forms a mixture with good ignitability from liquid fuel and supplies it to an internal combustion engine, making it possible to perform from cold start to steady operation of the internal combustion engine with a single fuel system. The present invention relates to a rapid evaporation device for liquid fuel for an internal combustion engine, and in particular to a rapid evaporation device for alcohol fuel.
従来のガソリン燃料に代替しアルコール燃料で火花点火
式力燃機関を運転する場合、キャブレタ。Carburetor when operating a spark-ignition power combustion engine with alcohol fuel instead of conventional gasoline fuel.
燃料噴射装置等を利用する燃料供給装置では冷間時には
着火可能な混合気を形成し得ない為にその始動が困難で
ある。このため、始動時のみガソリン燃料を併用し、内
燃機関の暖気運転後アルコール燃料に切換えるようにし
ており、従って、燃料及び燃料供給装置に二系統を必要
とし、ガソリン燃料で運転する場合に比して非常に不利
となっている。A fuel supply system that uses a fuel injection system or the like cannot form an ignitable air-fuel mixture when it is cold, making it difficult to start the system. For this reason, gasoline fuel is used only at the time of starting, and the engine is switched to alcohol fuel after it has been warmed up. Therefore, two systems are required for the fuel and fuel supply system, compared to when operating on gasoline fuel. This is extremely disadvantageous.
本発明は、アルコール燃料の噴霧粒径を微粒化すると共
に所要の混合比を有する混合気を形成することにより着
火性を向上させ、ガソリンエンジンに劣らぬ冷間始動性
を得ることを目的とする。The purpose of the present invention is to improve ignition performance by atomizing the spray particle size of alcohol fuel and forming a mixture having a required mixture ratio, thereby obtaining cold startability comparable to that of a gasoline engine. .
先ず、本発明の基本原理を説明する。普通燃料の蒸発に
要する熱量dQ及び時間Tは
dQ=c1 ・L・4zr2d r
T=02・a2 ・L
なる式で示されることが知られている。但し、C1及び
C2は燃料の物性9周囲温度等により規定される定数、
Lは蒸発潜熱、rは液滴半径、aは蒸発前の初期液滴径
である。First, the basic principle of the present invention will be explained. It is known that the amount of heat dQ and time T required for evaporation of normal fuel are expressed by the following formula: dQ=c1.L.4zr2d r T=02.a2.L. However, C1 and C2 are constants determined by physical properties of fuel 9 ambient temperature, etc.
L is the latent heat of vaporization, r is the droplet radius, and a is the initial droplet diameter before evaporation.
従って、熱量dQは液滴の表面積4πr2に支配される
ので、加熱する液滴が小粒子であるほど。Therefore, since the amount of heat dQ is controlled by the surface area 4πr2 of the droplet, the smaller the droplet to be heated, the more the smaller the droplet is.
効率的に加熱することができる。また時間Tも初期液滴
径aに支配されるので、加熱する液滴が小粒子であるほ
ど、短時間に蒸発することができる。It can be heated efficiently. Further, since the time T is also controlled by the initial droplet diameter a, the smaller the heated droplet, the faster it can evaporate.
更に蒸発潜熱りは燃料の圧力が高まるにつれて小さくな
ることが知られているので、燃料を小さな粒径の液滴状
にして高圧高温環境下で加熱することにより、短時間に
少ない熱量で蒸発させ、微粒化することが可能となる。Furthermore, it is known that the latent heat of vaporization decreases as the pressure of the fuel increases, so by forming fuel into small droplets and heating them in a high-pressure, high-temperature environment, it is possible to evaporate the fuel in a short time and with a small amount of heat. , it becomes possible to atomize the particles.
ところで、上述の原理に基づく液体燃料の急速蒸発装置
を実施するについて、冷間時にいかに小さな粒径の燃料
粒子を形成するか且ついかに均質な混合気を形成するか
が問題となる。By the way, when implementing a rapid evaporation device for liquid fuel based on the above-mentioned principle, the problem is how to form fuel particles with a small particle size and how to form a homogeneous air-fuel mixture when the fuel is cold.
しかしながら、単独の方法で上記の高温高圧環境を形成
し且つ均質で着火性の良い混合気を形成するにはシステ
ムが複雑なものとなりコストの高いものとならざるを得
なかった。However, in order to form the above-mentioned high-temperature, high-pressure environment and a homogeneous air-fuel mixture with good ignitability using a single method, the system must become complicated and costly.
本発明はエンジン温度が一20°C以下に低下する極寒
冷地においても冷間始動が可能となるようにし、且つ予
加熱装置、低圧噴射装置、及び熱面蒸発装置を有機的に
組合せてシステムを簡素化した液体燃料の急速蒸発装置
を提供するものである。The present invention enables cold starting even in extremely cold regions where the engine temperature drops below 120°C, and also organically combines a preheating device, a low pressure injection device, and a hot surface evaporation device. The present invention provides a liquid fuel rapid evaporation device that is simplified.
すなわち、本発明に依れば、予混合室内に設けられた熱
面蒸発装置の高温状態の熱面部に、低圧噴射装置により
所要の噴射量に制御された燃料を噴射吹き当てて蒸発さ
せ、空気調整弁により調量され予加熱装置により加熱さ
れた空気を前記予混室内に供給し、前記燃料粒子と空気
を所要の混合比に混合し、該混合気をエン゛ジンに吸入
させ、該エンジンの圧縮行程による高圧高温環境で前記
燃料粒子を急速に蒸発させるようにし、容易に冷間始動
させるようにしたものである。That is, according to the present invention, fuel controlled to a required injection amount is injected and evaporated by a low-pressure injection device onto the high-temperature hot surface portion of a hot surface evaporator provided in a premixing chamber, and air is evaporated. Air metered by a regulating valve and heated by a preheating device is supplied into the premixing chamber, the fuel particles and air are mixed at a required mixture ratio, and the mixture is sucked into the engine. The fuel particles are rapidly evaporated in a high-pressure, high-temperature environment during the compression stroke, making it easy to start cold.
以下本発明の一実施例を添付図面に基ついて説明する。An embodiment of the present invention will be described below with reference to the accompanying drawings.
図面は本発明の急速蒸発装置の構成を示す図であり、急
速蒸発装置1は吸入空気の予加熱装置2゜エンジン10
に通しる予混合室3.該予混合室3内の図上略中央上部
に配置された熱面部4aを有する熱面蒸発装置4.燃料
ポンプ5を介して燃料タンク6よりメタノール燃料の所
要量を予混合室3内に噴射する低圧噴射装置7.および
改質ガス発生装置8より得た改質ガスを定常運転時に予
混合室3内に噴射する改質ガス噴射装置9により構成さ
れている。The drawing shows the configuration of a rapid evaporator according to the present invention, in which the rapid evaporator 1 includes an intake air preheating device 2, an engine 10
3. A premixing chamber that passes through the A hot surface evaporator 4 having a hot surface portion 4a disposed approximately in the upper center of the premixing chamber 3 in the figure. A low-pressure injection device 7 for injecting the required amount of methanol fuel into the premixing chamber 3 from the fuel tank 6 via the fuel pump 5. and a reformed gas injection device 9 that injects the reformed gas obtained from the reformed gas generator 8 into the premixing chamber 3 during steady operation.
予混合室3の土壁にはエアクリーナ11.スロットルバ
ルブ12を介して吸気管13が、予混合室3の上部側壁
にはスロットルバルブ12の上流側の吸気管13より分
岐したバイパス14が夫々接続されており、バイパス1
4には空気調整弁15゜予加熱装置2が順次介在されて
いる。空気調整弁15はエンジン10の冷却水の温度に
よって作動する図示しないサーモスタットにより、吸気
管13よりバイパス14を介して吸入した空気の通過面
積を制御して該空気を調量するものであり、予加熱装置
2は例えば従来公知のP TCハニカムヒータ等を用い
て前記空気調整弁15で調量された空気を所要温度迄加
熱するものである。An air cleaner 11 is installed on the earthen wall of the premixing chamber 3. An intake pipe 13 is connected through the throttle valve 12, and a bypass 14 branched from the intake pipe 13 on the upstream side of the throttle valve 12 is connected to the upper side wall of the premixing chamber 3.
4, an air regulating valve 15° and a preheating device 2 are interposed in sequence. The air regulating valve 15 controls the passage area of the air taken in from the intake pipe 13 via the bypass 14 by a thermostat (not shown) that is activated depending on the temperature of the cooling water of the engine 10, and adjusts the amount of the air. The heating device 2 heats the air metered by the air regulating valve 15 to a required temperature using, for example, a conventionally known PTC honeycomb heater.
予混合室3内の略中央上部の熱面蒸発装置41ま例えば
温度上昇速度の大きいセラミックヒータを熱伝導率の高
い胴の薄板で被覆して形成された平板状の熱面部4aを
電気的に加熱することによって熱面部4aの表面温度を
所定の高温状態に保つようにしている。The hot surface evaporator 41 located approximately at the upper center of the premixing chamber 3 is electrically connected to a flat hot surface portion 4a formed by covering a ceramic heater with a high temperature rise rate with a thin body plate having high thermal conductivity. By heating, the surface temperature of the hot surface portion 4a is maintained at a predetermined high temperature.
予混合室3内の上部側壁には低圧噴射装置7カ玉メタノ
ール燃料噴射ロアaを前記熱面部4a4::対面させて
配設されており、メタノール燃料の噴射量の調整はコン
トロールユニット16で行う。すなわち、コントロール
ユニット16カ1水温センサ16a2回転数センサ16
b、ブースト圧センサ16cで夫々検知したエンジン1
0の冷却水温度。A low-pressure injection device 7 and a methanol fuel injection lower a are arranged on the upper side wall of the premixing chamber 3 so as to face the hot surface section 4a4, and the control unit 16 adjusts the injection amount of methanol fuel. . That is, 16 control units, 1 water temperature sensor 16a, 2 rotation speed sensors 16
b. Engine 1 detected by boost pressure sensor 16c.
0 cooling water temperature.
エンジン10の回転数、予混合室3内のブースト圧に基
づいて低圧噴射弁7bの開弁期間を演算制御することに
より上記噴射量の調整を行う。低圧噴射装置7としては
、例えばジェトロニック弁の一種で例えば、噴射圧力2
.5kg/cm2.噴射量380 cc/ min 、
平均粒径SMD=80pmの性能をもつシングルポイン
1へ・インジェクションに用いられるものが使用される
。The injection amount is adjusted by calculating and controlling the opening period of the low-pressure injection valve 7b based on the rotational speed of the engine 10 and the boost pressure in the premixing chamber 3. The low-pressure injection device 7 is, for example, a type of jetronic valve, for example, with an injection pressure of 2
.. 5kg/cm2. Injection amount 380 cc/min,
A material used for single point 1 injection with an average particle size SMD of 80 pm is used.
予混合室3の下方側部、即ちエンジンIO側部には改質
ガス噴射口9aを予混合室3内に臨ませて改質ガス噴射
装置9が配設され、エンジン10が暖気し定常運転に至
ると、前記低圧噴射装置の場合と同様にコントロールユ
ニット16が作用し改質ガス噴射弁9bを開弁じて所要
量の改質ガスが予混合室3内に噴射するようになってい
る。A reformed gas injection device 9 is disposed on the lower side of the premixing chamber 3, that is, on the engine IO side, with a reformed gas injection port 9a facing into the premixing chamber 3, and the engine 10 is warmed up and operated normally. When this occurs, the control unit 16 acts as in the case of the low-pressure injection device to open the reformed gas injection valve 9b and inject the required amount of reformed gas into the premixing chamber 3.
予混合室3は後述するように予混合室3内で形成された
メタノールと空気の混合気をエンジン10に供給するよ
うにされている。The premixing chamber 3 is configured to supply a mixture of methanol and air formed within the premixing chamber 3 to the engine 10, as will be described later.
上記構成において、エンジン10の冷間始動から暖機迄
の間はスロットバルブ12を閉弁し吸気管13より吸入
した空気をエアークリーナ11゜バイパス14を介して
バイパス14の開口14aより予混合室3内に流入させ
る。このとき前記バイパス空気は前述のように空気調整
弁15により所要の流量に調量され、予加熱装置2によ
り所定温度(例えば200℃)に加熱されて予混合室3
内の熱面部4aに接触し、所定温度(例えば200℃)
に加熱された熱面部4aによりその高温状態が維持され
る。In the above configuration, from cold start to warm-up of the engine 10, the slot valve 12 is closed and the air taken in from the intake pipe 13 is passed through the air cleaner 11° bypass 14 to the opening 14a of the bypass 14 to the premixing chamber. Let it flow into 3. At this time, the bypass air is regulated to a required flow rate by the air regulating valve 15 as described above, heated to a predetermined temperature (for example, 200° C.) by the preheating device 2, and then heated to the premixing chamber 3.
contact with the inner hot surface part 4a, and the predetermined temperature (e.g. 200°C)
The high-temperature state is maintained by the hot surface portion 4a that is heated.
一方、メタノール燃料は燃料タンク6より燃料ポンプ5
を介して低圧噴射装置7の噴射ロアaから予混合室3内
に噴射される。このとき前記メタノール燃料は前述した
ようにコントロールユニット16によって所要の噴射基
に制御されて前記熱面蒸発装置4の熱面部4aに吹き当
り、前記所定温度を有する熱面部4aの表面より蒸発し
微粒化されて前記バイパス空気と混合し所定の混合比の
混合気を形成する。On the other hand, methanol fuel is supplied to the fuel pump 5 from the fuel tank 6.
The fuel is injected into the premixing chamber 3 from the injection lower a of the low-pressure injection device 7 via. At this time, as described above, the methanol fuel is controlled by the control unit 16 at a required injection rate and is blown against the hot surface section 4a of the hot surface evaporator 4, and is evaporated from the surface of the hot surface section 4a having the predetermined temperature to form fine particles. The air is mixed with the bypass air to form a mixture having a predetermined mixing ratio.
前述のように高圧且つ所要の混合比に形成された前記メ
タノール粒子と前記空気との混合気は予混合室3からエ
ンジン10に供給され、エンジン10の断熱圧縮行程に
より前記メタノール燃料粒子が更に高温高圧化さオして
急速に蒸発し更に微粒化する。The mixture of the methanol particles and the air, which has been formed at high pressure and at a required mixing ratio as described above, is supplied to the engine 10 from the premixing chamber 3, and the methanol fuel particles are further heated to a high temperature by the adiabatic compression stroke of the engine 10. When the pressure is increased, it evaporates rapidly and becomes even more atomized.
エンジンの高負荷と全負荷時には、メタノールを気体化
すると体積が増加する為にエンジン吸気量か減少(例え
ば充填効率が50%程度まで下がる)してしまうので再
び生メタノールを供給して、前述の蒸発潜熱で内部冷却
することでエンジン吸気量を高め出力性能を改善するこ
とができる。When the engine is under high load or full load, when methanol is gasified, the volume increases and the engine intake air volume decreases (for example, the filling efficiency drops to about 50%), so raw methanol is supplied again and the above-mentioned By internally cooling the engine using latent heat of vaporization, it is possible to increase the amount of intake air in the engine and improve output performance.
次にエンジン10が暖機し定常運転に至ると前述の如く
コントロールユニット16の作用により低圧噴射弁7b
が閉弁すると共に改質ガス噴射弁9bが開弁じ、改質ガ
ス発生装置8により得られた改質ガスが改質ガス噴射口
9aより予混合室3内に噴射される。このときスロット
ルバルブ12を開弁じて吸気Iv13より吸入した空気
を直接予混合室3内に流入させ、前記改質ガスと該空気
との混合気を形成する。このようにして定常運転時には
改質ガスと空気との混合気をエンジン1oに供給するこ
とによってエンジン10の熱効率を高めることができる
。Next, when the engine 10 warms up and reaches steady operation, the low pressure injection valve 7b is activated by the action of the control unit 16 as described above.
is closed, and the reformed gas injection valve 9b is opened, and the reformed gas obtained by the reformed gas generator 8 is injected into the premixing chamber 3 from the reformed gas injection port 9a. At this time, the throttle valve 12 is opened to allow the air taken in from the intake Iv13 to directly flow into the premixing chamber 3, thereby forming a mixture of the reformed gas and the air. In this manner, the thermal efficiency of the engine 10 can be increased by supplying the mixture of reformed gas and air to the engine 1o during steady operation.
尚、本実施例においては燃料をメタノール燃料の場合に
ついて記述したがこれに限るものではなく、ガソリンを
燃料として使用することもできる。Although the present embodiment has been described using methanol as the fuel, the present invention is not limited to this, and gasoline may also be used as the fuel.
以上説明したように本発明によれば、予混合室内に設け
られた熱面蒸発装置の高温状態の熱面部に、低圧噴射装
置により所要の噴射量に制御された燃料を噴射吹き当て
て蒸発させ、空気調整弁により調量され予加熱装置によ
り、加熱された空気を前記予混合室内に供給し、前記燃
料粒子と空気を所要の混合比に混合し、該混合気をエン
ジンに吸入させ、該エンジンの圧縮行程による高圧高温
環境で前記燃料粒子を急速に蒸発させることにより極寒
冷地においても容易にエンジンの冷間始動が可能となる
。また、空気の予加熱装置、燃料の熱面蒸発装置、及び
燃料の低圧噴射装置の三方式を一体にしたことにより装
置の構成が簡単となり、製造コストが低減する。As explained above, according to the present invention, fuel controlled to a required injection amount by a low-pressure injection device is injected and evaporated onto the high-temperature hot surface portion of the hot surface evaporator provided in the premixing chamber. , the amount of air adjusted by the air regulating valve and heated by the preheating device is supplied into the premixing chamber, the fuel particles and air are mixed at a required mixing ratio, the mixture is sucked into the engine, and the air is heated by the preheating device. By rapidly evaporating the fuel particles in a high-pressure, high-temperature environment during the engine's compression stroke, the engine can be easily cold-started even in extremely cold regions. Further, by integrating the three systems of the air preheating device, the fuel hot surface evaporation device, and the fuel low-pressure injection device, the configuration of the device is simplified and manufacturing costs are reduced.
また、全負荷時に液体メタノール燃料を使用すれば、気
化したメタノールの体積増加に伴なうエンジン吸気量の
減少に対してエンジン吸気量を高め、エンジンの性能を
高めることができ(略110%)、エンジン暖機後の定
常運転時においてはメタノール燃料の改質ガスを用いる
ことによりエンジンの熱効率を高めることができる(略
50%)。In addition, if liquid methanol fuel is used at full load, the engine intake volume can be increased to compensate for the decrease in engine intake volume due to the increase in volume of vaporized methanol, and engine performance can be improved (approximately 110%). During steady operation after warming up the engine, the thermal efficiency of the engine can be increased (approximately 50%) by using reformed methanol fuel gas.
更に、ガソリン燃料を使用すれば、エンジンの始動から
暖機完了迄は適正混合比で運転できるのでエミッシ曹ン
と燃費の大幅改善ができる。Furthermore, if gasoline fuel is used, the engine can be operated at a proper mixture ratio from the start of the engine until it is warmed up, resulting in a significant improvement in emissions and fuel efficiency.
図面は本発明に係る液体燃料の急速蒸発装置の一実施例
の構成を示す図である。
l・・・急速蒸発装置、2・・・予加熱装置、3・・・
予混合室、4・・・熱面蒸発装置、4a・・・熱面部、
7・・・低圧噴射装置、lO・・・エンジン、15・・
・空気調整弁。
出願人 ヂーゼル機器株式会社
代理人 弁理士 渡部敏彦The drawing is a diagram showing the configuration of an embodiment of a rapid evaporation device for liquid fuel according to the present invention. 1... Rapid evaporator, 2... Preheating device, 3...
Premixing chamber, 4... Hot surface evaporator, 4a... Hot surface section,
7...Low pressure injection device, lO...engine, 15...
・Air adjustment valve. Applicant: Diesel Kiki Co., Ltd. Agent: Patent Attorney: Toshihiko Watanabe
Claims (1)
熱面部に、低圧噴射装置により所要の噴射量に制御され
た燃料を噴射吹き当てて蒸発させ、空気調整弁により調
量され予加熱装置により加熱された空気を前記予混合室
内に供給し、前記燃料粒子と空気を所要の混合比に混合
し、該混合気をエンジンに吸入させ、該エンジンの圧縮
行程による高圧高温環境で前記燃料粒子を急速に蒸発さ
せるようにしたことを特徴とする液体燃料の急速蒸発装
置。1. A low-pressure injection device injects and evaporates fuel, which is controlled to the required injection amount, onto the high-temperature hot surface of the hot surface evaporator installed in the premixing chamber. Air heated by a heating device is supplied into the premixing chamber, the fuel particles and air are mixed at a required mixture ratio, the mixture is sucked into the engine, and the mixture is heated in a high pressure and high temperature environment due to the compression stroke of the engine. A rapid evaporation device for liquid fuel characterized by rapidly evaporating fuel particles.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP57146581A JPS5937267A (en) | 1982-08-24 | 1982-08-24 | Quick evaporation device for liquid fuel |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP57146581A JPS5937267A (en) | 1982-08-24 | 1982-08-24 | Quick evaporation device for liquid fuel |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS5937267A true JPS5937267A (en) | 1984-02-29 |
Family
ID=15410931
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP57146581A Pending JPS5937267A (en) | 1982-08-24 | 1982-08-24 | Quick evaporation device for liquid fuel |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5937267A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1994010439A1 (en) * | 1992-11-03 | 1994-05-11 | Gentec B.V. | Mixing/metering unit |
-
1982
- 1982-08-24 JP JP57146581A patent/JPS5937267A/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1994010439A1 (en) * | 1992-11-03 | 1994-05-11 | Gentec B.V. | Mixing/metering unit |
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