JPS5831452B2 - Nenshiyoukikan - Google Patents

Nenshiyoukikan

Info

Publication number
JPS5831452B2
JPS5831452B2 JP50038927A JP3892775A JPS5831452B2 JP S5831452 B2 JPS5831452 B2 JP S5831452B2 JP 50038927 A JP50038927 A JP 50038927A JP 3892775 A JP3892775 A JP 3892775A JP S5831452 B2 JPS5831452 B2 JP S5831452B2
Authority
JP
Japan
Prior art keywords
fuel
methanol
auxiliary burner
combustion engine
inner cylinder
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
Application number
JP50038927A
Other languages
Japanese (ja)
Other versions
JPS51113004A (en
Inventor
勝明 小坂
善衛 上野
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.)
Nissan Motor Co Ltd
Original Assignee
Nissan Motor 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 Nissan Motor Co Ltd filed Critical Nissan Motor Co Ltd
Priority to JP50038927A priority Critical patent/JPS5831452B2/en
Priority to GB10451/76A priority patent/GB1521224A/en
Priority to DE2613348A priority patent/DE2613348B2/en
Priority to FR7608996A priority patent/FR2306343A1/en
Publication of JPS51113004A publication Critical patent/JPS51113004A/en
Publication of JPS5831452B2 publication Critical patent/JPS5831452B2/en
Expired legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02BINTERNAL-COMBUSTION PISTON ENGINES; COMBUSTION ENGINES IN GENERAL
    • F02B1/00Engines characterised by fuel-air mixture compression
    • F02B1/02Engines characterised by fuel-air mixture compression with positive ignition
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02BINTERNAL-COMBUSTION PISTON ENGINES; COMBUSTION ENGINES IN GENERAL
    • F02B43/00Engines characterised by operating on gaseous fuels; Plants including such engines
    • F02B43/10Engines or plants characterised by use of other specific gases, e.g. acetylene, oxyhydrogen
    • 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
    • F02M27/00Apparatus for treating combustion-air, fuel, or fuel-air mixture, by catalysts, electric means, magnetism, rays, sound waves, or the like
    • F02M27/02Apparatus for treating combustion-air, fuel, or fuel-air mixture, by catalysts, electric means, magnetism, rays, sound waves, or the like by catalysts
    • 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)
  • Output Control And Ontrol Of Special Type Engine (AREA)
  • Exhaust Gas After Treatment (AREA)
  • Combustion Methods Of Internal-Combustion Engines (AREA)
  • Cylinder Crankcases Of Internal Combustion Engines (AREA)

Description

【発明の詳細な説明】 本発明はメタノールを接触分解し、COとH2を主成分
とするガス燃料に改質し、この改質ガス燃料を機関で燃
焼させること(こより、過薄混合気での運転を円滑なら
しめ有害排気ガス成分の低減と燃費の向上を図った燃焼
機関に関する。
Detailed Description of the Invention The present invention involves catalytically cracking methanol, reforming it into a gaseous fuel whose main components are CO and H2, and combusting this reformed gaseous fuel in an engine. This invention relates to a combustion engine that enables smooth operation, reduces harmful exhaust gas components, and improves fuel efficiency.

本発明はメタノールの一部あるいは全部を接触分解して
H2とCOに富むガス燃料に効率よく改質することので
きる改質装置を備えた燃焼機関を得るにある。
The object of the present invention is to obtain a combustion engine equipped with a reformer that can catalytically crack part or all of methanol to efficiently reform it into a gaseous fuel rich in H2 and CO.

以下、図面に示す実施例(こより本発明の詳細な説明す
る。
Hereinafter, the present invention will be described in detail from the embodiments shown in the drawings.

第1図において、1は燃焼機関としての内燃機関で、こ
の内燃機関1はシリンダ2が形成されたシリンダブロッ
ク3と、このシリンダブロック3のシリンダ2内を往復
動するピストン4と、シリンダブロック3にガスケット
等を介してボルト締め固定されたシリンダヘッド5と、
シリンダヘッド5に形成された燃焼室6と吸気弁7を介
して連通された吸気孔8および燃焼室6と排気弁9を介
して連通された排気孔10と、この排気孔10に連通さ
れた排気管11と、この排気管11中に介挿された燃料
改質装置12と、この燃料改質装置12で改質された燃
料がパイプ13、混合器14を介して供給される吸気孔
8に連通された吸気管14aとから構成されている。
In FIG. 1, 1 is an internal combustion engine as a combustion engine, and this internal combustion engine 1 includes a cylinder block 3 in which a cylinder 2 is formed, a piston 4 that reciprocates within the cylinder 2 of this cylinder block 3, and a cylinder block 3. A cylinder head 5 is bolted and fixed via a gasket or the like to the cylinder head 5,
An intake hole 8 communicates with a combustion chamber 6 formed in the cylinder head 5 via an intake valve 7, and an exhaust hole 10 communicates with the combustion chamber 6 via an exhaust valve 9. An exhaust pipe 11, a fuel reformer 12 inserted into the exhaust pipe 11, and an intake hole 8 to which fuel reformed by the fuel reformer 12 is supplied via a pipe 13 and a mixer 14. The intake pipe 14a is connected to the intake pipe 14a.

また燃料改質装置12は排気孔11と連通された内筒1
5と、この内筒15の外周に所定間隔へだてて備えられ
た外筒16と、この外筒16と内筒15とにより形成さ
れた触媒室17aと、触媒室17aに挿入された触媒1
7と、一端が弁18、ポンプ19を介してメタノール2
0が入れられたタンク21に接続され、他端が内筒15
内で充分熱せられるようζこ配されて前記触媒室17a
内に接続されたメタノール供給パイプ22と、内筒15
の上流側に備えられた点介栓付の補助バーナー23と、
この補助バーナー23ヘメタノールを供給する弁24を
介してポンプ19に接続されたパイプ25と、補助バー
ナー23へ空気を供給するブロアー26とから構成され
ている。
Further, the fuel reformer 12 has an inner cylinder 1 that communicates with the exhaust hole 11.
5, an outer cylinder 16 provided at a predetermined interval on the outer circumference of the inner cylinder 15, a catalyst chamber 17a formed by the outer cylinder 16 and the inner cylinder 15, and a catalyst 1 inserted in the catalyst chamber 17a.
7, one end is supplied with methanol 2 through a valve 18 and a pump 19.
0 is placed in the tank 21, and the other end is connected to the inner cylinder 15.
The catalyst chamber 17a is arranged so that it can be sufficiently heated within the catalyst chamber 17a.
methanol supply pipe 22 connected to the inner cylinder 15;
an auxiliary burner 23 with a point stopper provided on the upstream side of the
It is comprised of a pipe 25 connected to the pump 19 via a valve 24 for supplying methanol to the auxiliary burner 23, and a blower 26 for supplying air to the auxiliary burner 23.

上記構成のものにあっては補助バーナー23ヘタンク2
1よりメタノール20をメタノール供給パイプ22、ポ
ンプ19ぢ弁24を介してパイプ25より供給するとと
もQこブロアー26によって空気を供給して点火のうえ
燃焼させ触媒17の温度をメタノール分解温度(300
〜400’C)に達するまで燃焼させる。
In the case of the above configuration, the auxiliary burner 23 is connected to the tank 2.
1, methanol 20 is supplied from a pipe 25 via a methanol supply pipe 22, a pump 19 and a valve 24, and air is supplied by a Q blower 26 to ignite and burn it, and the temperature of the catalyst 17 is set to the methanol decomposition temperature (300
Burn until reaching ~400'C).

これによりポンプ19、弁18を介してメタノール供給
パイプ22によって触媒室17a内へ供給されたメタノ
ールは自らがH2とCOに富むガス燃料に分解改質され
、混合気14へ供給される。
As a result, methanol supplied into the catalyst chamber 17a by the methanol supply pipe 22 via the pump 19 and the valve 18 is decomposed and reformed into a gaseous fuel rich in H2 and CO, which is then supplied to the air-fuel mixture 14.

この状態で内燃機関1をクランキングして始動させると
混合気14より空気と混合され吸気孔8より吸気弁7を
介して燃焼室6へ供給される。
When the internal combustion engine 1 is cranked and started in this state, the air-fuel mixture 14 is mixed with air and supplied to the combustion chamber 6 through the intake hole 8 and the intake valve 7 .

なお、この実施例の燃焼室(こは図示していないが点火
栓がありこれで混合気に点火することは通常の火花点火
式機関と同一である。
Note that the combustion chamber of this embodiment has an ignition plug (not shown) and ignites the air-fuel mixture using this, which is the same as in a normal spark ignition type engine.

そして、この燃焼室6で燃焼された排気ガスは排気弁9
を介して排気孔10および排気管11へ排出される。
The exhaust gas combusted in this combustion chamber 6 is then transferred to an exhaust valve 9.
It is discharged to the exhaust hole 10 and the exhaust pipe 11 through the exhaust hole 10 and the exhaust pipe 11.

この排気ガスが排気管11中に介挿された燃料改質装置
12を加熱することとなる。
This exhaust gas heats the fuel reformer 12 inserted into the exhaust pipe 11.

このため補助バーナー23の燃焼はその分だけ小さくす
る。
Therefore, the combustion of the auxiliary burner 23 is reduced accordingly.

なお、排気温度が高くて補助バーナー23を止めても燃
料改質装置12が高温になる場合には、補助バーナー2
3より空気だけを内筒内へ供給して触媒17を冷却し改
質適温に保つ。
In addition, if the exhaust temperature is high and the fuel reformer 12 becomes high temperature even if the auxiliary burner 23 is stopped, the auxiliary burner 2
3, only air is supplied into the inner cylinder to cool the catalyst 17 and keep it at an appropriate temperature for reforming.

また、内燃機関運転時は通常空気過剰率λ=2程度で運
転しているので、排気中の残存酸素の利用により補助バ
ーナー23ヘメタノールだけを供給してブロアー26を
停止してもよい。
Furthermore, since the internal combustion engine is normally operated at an excess air ratio λ of approximately 2, the blower 26 may be stopped by supplying only methanol to the auxiliary burner 23 by utilizing the residual oxygen in the exhaust gas.

さらに、また改質ガスと残余燃料すなわち改質していな
いメタノール燃料との混合物を燃焼機関に供給すること
により過薄混合気での運転を円滑ならしめることができ
る。
Furthermore, by supplying a mixture of reformed gas and residual fuel, that is, unreformed methanol fuel, to the combustion engine, smooth operation with a lean mixture can be achieved.

次に第2図に示す第2番目の発明の、実施例につき説明
する。
Next, an embodiment of the second invention shown in FIG. 2 will be described.

なお、この実施例の説明に当って機能上前記実施例のも
のと同−又は均等構成と考えられる部分ζこは前記実施
例と同一符号を付して重複する説明を省略する。
In the description of this embodiment, parts ζ that are considered to have the same or equivalent structure as those of the previous embodiment in terms of function will be designated by the same reference numerals as those of the previous embodiment, and redundant explanation will be omitted.

第2図の実施例(こおいて、前記第1図の実施例と主に
異なる点はパイプ13中に改質ガスを冷却するコンデン
サー27と、このコンデンサー27の下流に備えられた
気液分離器28と、この気液分離器28からガス成分を
混合気14へ供給するとともに凝縮成分を補助バーナー
23ヘポンプ29、弁30を介してパイプ31で供給で
きるようにした点で、このように構成することにより、
未分解(20〜30%)のメタノールやホルムアルデヒ
ド、ギ酸メチル等の物質を補助バーナー23で燃焼でき
る。
The embodiment shown in FIG. 2 (here, the main differences from the embodiment shown in FIG. This configuration is such that gas components can be supplied from the gas-liquid separator 28 to the mixture 14 and condensed components can be supplied to the auxiliary burner 23 via a pump 29 and a valve 30 and a pipe 31. By doing so,
Substances such as undecomposed (20 to 30%) methanol, formaldehyde, methyl formate, etc. can be burned in the auxiliary burner 23.

したがって前記の物質による各機器への悪影響を効率よ
く防止できる。
Therefore, it is possible to efficiently prevent the adverse effects of the above-mentioned substances on each device.

その理由は以下のとおりである。The reason is as follows.

改質装置によるメタノール分解生成物中には、燃焼し難
いメタノールやホルムアルデヒド等の凝縮成分が含まれ
ており、もしこれらを機関へ送ると、どうしても凝縮成
分が混合気の計量部は勿論、燃焼室(間欠燃焼であるか
ら低温の時もある)その他機関の各機器へ耐着し、機関
の性能を害する傾向がある。
The methanol decomposition product from the reformer contains condensed components such as methanol and formaldehyde, which are difficult to burn.If these are sent to the engine, the condensed components will not only enter the air-fuel mixture metering section but also the combustion chamber. (Because it is an intermittent combustion, there are times when the temperature is low.) It tends to adhere to other engine equipment and harm the performance of the engine.

そこで第2番目の発明では凝縮成分を分離してこれを補
助バーナーの燃料として用いるものであり、このように
すると排気系は各気筒の排気の集合部であると共に高温
の膨張ガスが流通しているため、はぼ連続燃焼系とみな
し得るので、機関燃焼室では燃え難い前記成分を確実に
燃焼して各機器への悪影響を防止できるのである。
Therefore, in the second invention, the condensed component is separated and used as fuel for the auxiliary burner.In this way, the exhaust system serves as a collection point for the exhaust gas from each cylinder and also as a place where high-temperature expanded gas flows. Therefore, it can be regarded as a continuous combustion system, and the components that are difficult to burn in the engine combustion chamber can be reliably burned to prevent adverse effects on various devices.

以上の説明から明らかなように本発明によればメタノー
ルの一部あるいは全部を接触分解してH2とCOに富む
ガス燃料に効率よく改質できるので、燃焼機関へ充分(
こ供給でき過薄混合気での運転を円滑ならしめるととも
(こ排気ガス中に含まれる有害成分を低減できかつ燃費
の向上を図ることができる。
As is clear from the above description, according to the present invention, part or all of methanol can be catalytically cracked and efficiently reformed into a gaseous fuel rich in H2 and CO.
By supplying this fuel, it is possible to smoothen operation with a lean mixture (this can reduce harmful components contained in exhaust gas and improve fuel efficiency).

また補助バーナーで燃料改質装置を加熱するので、定常
運転時には分解熱の不足分を補うことができるとともに
始動時には暖機時間を短縮できる利点がある。
In addition, since the fuel reformer is heated by the auxiliary burner, it is possible to make up for the lack of decomposition heat during steady operation, and there is an advantage that the warm-up time can be shortened during startup.

さらにメタノール分解生成物中の凝縮成分を補助バーナ
ーで優先的に燃焼させるよう(こしたので、ホルムアル
デヒド等の中間生成物の滞留を防止して各機器への悪影
響を防止できる等の優れた利点がある。
Furthermore, the condensed components in the methanol decomposition products are preferentially combusted by the auxiliary burner, which has excellent advantages such as preventing the accumulation of intermediate products such as formaldehyde and preventing adverse effects on various equipment. be.

なお、本発明は火花点火式機関はもちろん、圧縮着火式
機関にも適用できる。
Note that the present invention is applicable not only to spark ignition engines but also to compression ignition engines.

【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概略説明図、第2図は
第1図とは異なる実施例を示す概略説明図である。 1・・・・・・燃焼機関としての内燃機関、2・・・・
・・シリンダ、3・・・・・・シリンダブロック、4・
・・・・・ピストン、5・・・・・・シリンダヘッド、
6・・・・・・燃焼室、7・・・・・・吸気弁、8・・
・・・・吸気孔、9・・・・・・排気弁、10・・・・
・・排気孔、11・・・・・・排気管、12・・・・・
・燃料改質装置、13・・・・・・パイプ、14・・・
・・・混合器、14a・・・・・・吸気管、15・・・
・・・内筒、16・・・・・・外筒、17・・・・・・
触媒、17a・・・・・・触媒室、18・・・・・・弁
、19・・・・・・ポンプ、20・・・・・・メタノー
ル、21・・・・・・タンク、22・・・・・・メタノ
ール供給パイプ、23・・・・・・補助バーナ、24・
・・・・・弁、25・・・・・・パイプ、26・・・・
・・ブロアー、27・・・・・・コンデンサー、28・
・・・・・気液分離器、29・・・・・・ポンプ、30
・・・・・・弁、31・・・・・・パイプO
FIG. 1 is a schematic explanatory diagram showing one embodiment of the present invention, and FIG. 2 is a schematic explanatory diagram showing an embodiment different from FIG. 1. 1... Internal combustion engine as a combustion engine, 2...
...Cylinder, 3...Cylinder block, 4.
... Piston, 5 ... Cylinder head,
6... Combustion chamber, 7... Intake valve, 8...
...Intake hole, 9...Exhaust valve, 10...
...Exhaust hole, 11...Exhaust pipe, 12...
・Fuel reformer, 13...pipe, 14...
...Mixer, 14a...Intake pipe, 15...
...Inner cylinder, 16...Outer cylinder, 17...
Catalyst, 17a... Catalyst chamber, 18... Valve, 19... Pump, 20... Methanol, 21... Tank, 22... ...Methanol supply pipe, 23...Auxiliary burner, 24.
...Valve, 25...Pipe, 26...
...Blower, 27...Condenser, 28.
...gas-liquid separator, 29 ...pump, 30
... Valve, 31 ... Pipe O

Claims (1)

【特許請求の範囲】 1 メタノールの一部あるいは全部を改質装置によって
接触分解して水素(H2)と−酸化炭素(CO)に富む
ガス燃料(こ改質し、この改質ガスあるいは改質ガスと
残余燃料との混合物を燃料とする燃焼機関において、前
記改質装置は、前記燃焼機関の排気管中に介挿された内
筒と、この内筒の外周(こ所定間隔へだてて備えられた
外筒と、この外筒と前記内筒とにより形成された触媒室
と、この触媒室に挿入さえた触媒と、一端がメタノール
タンクに接続され他端が前記内筒内で排気により熱せら
れるように配されて前記触媒室に接続されたメタノール
供給パイプと、一端が前記触媒室に接続され改質された
燃料を前記燃焼機関の吸気系へ送るパイプと、前記内筒
の上流側に備えられた補助バーナーと、この補助バーナ
ーへ燃料を供給する装置と、この補助バーナーへ空気を
供給する装置とから構成され、前記改質装置の接触分解
に必要な熱として前記燃焼機関の排気熱を利用するとと
もに、前記燃焼機関の始動時及び排気温度の低い運転時
には、前記補助バーナーへ前記燃料を供給する装置(こ
より燃料を供給し、排気温度の高い運転時には前記空気
を供給する装置により空気のみを供給するようにしたこ
とを特徴とする燃焼機関。 2、特許請求の範囲第1項記載の燃焼機関ζこおいて、
改質装置からメタノール分解生成物を機関へ送る管系中
に、メタノール分解生成物を冷却してそのガス成分を機
関の燃料として供給し、冷却により分離生成された凝縮
成分を補助バーナーの燃料として供給する装置を設けた
ことを特徴とする燃焼機関。
[Claims] 1 Part or all of methanol is catalytically cracked in a reformer to reform a gaseous fuel rich in hydrogen (H2) and carbon oxide (CO), and this reformed gas or reformed gas is reformed. In a combustion engine that uses a mixture of gas and residual fuel as fuel, the reformer includes an inner cylinder inserted into an exhaust pipe of the combustion engine, and an outer periphery of the inner cylinder (which is provided at a predetermined interval). a catalyst chamber formed by the outer cylinder and the inner cylinder, a catalyst inserted into the catalyst chamber, one end of which is connected to a methanol tank, and the other end of which is heated by exhaust gas within the inner cylinder. a methanol supply pipe arranged as shown in FIG. The system consists of an auxiliary burner, a device for supplying fuel to the auxiliary burner, and a device for supplying air to the auxiliary burner. At the same time, when the combustion engine is started or when the exhaust gas temperature is low, the fuel is supplied to the auxiliary burner by the device that supplies the fuel, and when the exhaust gas temperature is high, the air supply device is used to supply only air. 2. The combustion engine ζ according to claim 1, wherein:
In the pipe system that transports the methanol decomposition product from the reformer to the engine, there is a system in which the methanol decomposition product is cooled and its gas components are supplied as fuel for the engine, and the condensed components separated by cooling are used as fuel for the auxiliary burner. A combustion engine characterized by being equipped with a supply device.
JP50038927A 1975-03-31 1975-03-31 Nenshiyoukikan Expired JPS5831452B2 (en)

Priority Applications (4)

Application Number Priority Date Filing Date Title
JP50038927A JPS5831452B2 (en) 1975-03-31 1975-03-31 Nenshiyoukikan
GB10451/76A GB1521224A (en) 1975-03-31 1976-03-16 Combustion engine system
DE2613348A DE2613348B2 (en) 1975-03-31 1976-03-29 Fuel processing and conveying system of an internal combustion engine
FR7608996A FR2306343A1 (en) 1975-03-31 1976-03-29 COMBUSTION ENGINE POWER SUPPLY

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP50038927A JPS5831452B2 (en) 1975-03-31 1975-03-31 Nenshiyoukikan

Publications (2)

Publication Number Publication Date
JPS51113004A JPS51113004A (en) 1976-10-05
JPS5831452B2 true JPS5831452B2 (en) 1983-07-06

Family

ID=12538849

Family Applications (1)

Application Number Title Priority Date Filing Date
JP50038927A Expired JPS5831452B2 (en) 1975-03-31 1975-03-31 Nenshiyoukikan

Country Status (4)

Country Link
JP (1) JPS5831452B2 (en)
DE (1) DE2613348B2 (en)
FR (1) FR2306343A1 (en)
GB (1) GB1521224A (en)

Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4216751A (en) * 1976-04-26 1980-08-12 Davison Richard R Pre-vaporizing fuel system
BR8101247A (en) * 1981-02-27 1982-11-16 Antonio Filho Vivacqua EXPLOSION ENGINE AND APPLIANCE FOR THE CATALYTIC TRANSFER OF ALCOHOL AND / OR HYDROCARBONS AND THEIR MIXTURES IN COMBUSTIBLE FUEL GASES
JPS57153952A (en) * 1981-03-19 1982-09-22 Nissan Motor Co Ltd Starting device of alcohol engine
JPH0388957A (en) * 1989-08-22 1991-04-15 New Zealand Government Fuel feeder and controller of compressed ignition engine
EP0419743A1 (en) * 1989-09-29 1991-04-03 Her Majesty The Queen In Right Of New Zealand Fuel supply and control system for compression ignition engines
WO1993006358A1 (en) * 1991-09-18 1993-04-01 Alexandr Vasilievich Pugachev Method and device for preparation of fuel-air mixture for internal combustion engine
DE69910334T2 (en) 1998-03-26 2004-06-24 Pugachev, Aleksandr Vasilievič METHOD AND DEVICE FOR TREATING AN AIR-FUEL MIXTURE FOR INTERNAL COMBUSTION ENGINES AND HEAT EXCHANGERS

Also Published As

Publication number Publication date
GB1521224A (en) 1978-08-16
FR2306343B1 (en) 1981-04-10
DE2613348B2 (en) 1980-07-03
JPS51113004A (en) 1976-10-05
DE2613348A1 (en) 1976-10-14
FR2306343A1 (en) 1976-10-29

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