JPH0448938B2 - - Google Patents
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- Publication number
- JPH0448938B2 JPH0448938B2 JP59024386A JP2438684A JPH0448938B2 JP H0448938 B2 JPH0448938 B2 JP H0448938B2 JP 59024386 A JP59024386 A JP 59024386A JP 2438684 A JP2438684 A JP 2438684A JP H0448938 B2 JPH0448938 B2 JP H0448938B2
- Authority
- JP
- Japan
- Prior art keywords
- fuel
- oxygen
- dissolved
- peroxide
- engine
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
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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
- F02M25/00—Engine-pertinent apparatus for adding non-fuel substances or small quantities of secondary fuel to combustion-air, main fuel or fuel-air mixture
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F02—COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
- F02B—INTERNAL-COMBUSTION PISTON ENGINES; COMBUSTION ENGINES IN GENERAL
- F02B3/00—Engines characterised by air compression and subsequent fuel addition
- F02B3/06—Engines characterised by air compression and subsequent fuel addition with compression ignition
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Feeding And Controlling Fuel (AREA)
- Liquid Carbonaceous Fuels (AREA)
Description
【発明の詳細な説明】
技術分野
本発明はデイーゼルエンジン燃料の燃焼性の改
良方法に関し、詳しくは、デイーゼルエンジン用
の液体燃料に酸素を予め加圧溶解し、次いで酸化
触媒と接触させることにより、該燃料油を部分酸
化して燃料中にパーオキサイドを生成させ、これ
をデイーゼルエンジンで燃焼させることにより、
燃料油の着火性を改良し、あわせて該燃料油中の
溶解酸素を増すことで排気中の黒煙発生量をも低
下させ得る燃焼性の改良方法に関するものであ
る。DETAILED DESCRIPTION OF THE INVENTION Technical Field The present invention relates to a method for improving the combustibility of diesel engine fuel, and more specifically, by dissolving oxygen in advance under pressure in a liquid fuel for a diesel engine and then bringing it into contact with an oxidation catalyst, By partially oxidizing the fuel oil to generate peroxide in the fuel, and burning this in a diesel engine,
The present invention relates to a method for improving combustibility that can reduce the amount of black smoke generated in exhaust gas by improving the ignitability of fuel oil and increasing dissolved oxygen in the fuel oil.
従来技術
デイーゼルエンジンは、トラツク、バス、産業
機械、発電設備、船舶等に広く採用され、最近で
は乗用車への採用も増加し、これらにデイーゼル
エンジンに使用される軽油又は重油燃料の需要量
も増加している。このため石油精製工業等におい
て、限られた原油からこれら液体燃料の生産量を
増大させるために、蒸留の終点温度を高め収率を
増大する手段、重油の接触分解装置や熱分解装置
等で生産する分解油の利用等の検討が進められて
いる。大型船舶には、アスフアルトあるいは分解
装置における残渣油等の重質油の混合割合を増大
したバンカー重油あるいはコークス生産時に副生
するコールタール油等の利用も検討が進められて
いる。これら液体燃料は、直留型軽油あるいは重
油に比べ、炭素/水素(C/H)比が高く、排気
中の黒煙を増大させるとともに、セタン価も低い
ため安定な着火が困難である。Conventional technology Diesel engines are widely used in trucks, buses, industrial machinery, power generation equipment, ships, etc., and recently their use in passenger cars has also increased, and the demand for light oil or heavy oil fuel used in diesel engines has also increased. are doing. For this reason, in the petroleum refining industry, in order to increase the production of these liquid fuels from limited crude oil, methods of increasing the end point temperature of distillation and increasing the yield, production using heavy oil catalytic cracking equipment, thermal cracking equipment, etc. Studies are underway on the use of cracked oil. For large ships, the use of bunker heavy oil with an increased mixing ratio of heavy oil such as asphalt or residual oil from cracking equipment, or coal tar oil, which is a by-product during coke production, is also being considered. These liquid fuels have a higher carbon/hydrogen (C/H) ratio than straight-run light oil or heavy oil, which increases black smoke in the exhaust gas, and also have a low cetane number, making stable ignition difficult.
デイーゼルエンジン燃料の着火性すなわちセタ
ン価を向上するために、アミルナイトレートなど
のニトロ化合物系のセタン価向上剤が報告されて
いるが、多量の添加が必要であり、経済的でな
い。またパーオキサイドがセタン価向上の作用か
あることが知られているが、パーオキサイドは、
それ自信安定性が悪く、かつ強い酸化作用を有す
るため、製油所などで燃料を製造する際にこれを
添加して出荷すると、輸送中や貯蔵中にパーオキ
サイドにより燃料油が酸化劣化し、スラツジ生成
の原因になるため、実用が困難である。 In order to improve the ignitability, that is, the cetane number, of diesel engine fuel, nitro compound-based cetane number improvers such as amyl nitrate have been reported, but they require addition in large amounts and are not economical. It is also known that peroxide has the effect of improving the cetane number, but peroxide
It has poor stability and has a strong oxidizing effect, so if it is added to fuel at a refinery and shipped, the peroxide will oxidize and deteriorate the fuel oil during transportation and storage, resulting in sludge. It is difficult to put it into practical use because it causes generation.
エンジン運転中に燃料を改質して供給するシス
テムとしては、特開昭50−144816号公報に、軽油
を400〜800℃の高温条件下で改質して、水素、一
酸化炭素、メタン、メタノール等とパーオキサイ
ドを含む軽油とし、これらをエンジンの吸入空気
系に供給する熱機関が提案されている。しかしな
がらこのシステムでは、メタノールの生成がかえ
つてセタン価を低下させるため実用的でない。 As for a system for reforming and supplying fuel during engine operation, Japanese Patent Application Laid-open No. 144816/1984 describes a system that reformes diesel oil under high temperature conditions of 400 to 800°C to produce hydrogen, carbon monoxide, methane, etc. A heat engine has been proposed that uses light oil containing methanol etc. and peroxide and supplies these to the intake air system of the engine. However, this system is not practical because the production of methanol actually reduces the cetane number.
しかして本願発明者等は、先に低質な燃料を着
火性良く燃焼させる方法として、飽和炭化水素を
主成分とする副燃料を90〜220℃程度の低温で接
触部分酸化してパーオキサイドを含有させた燃料
に変換し、これを主燃料と併用して、デイーゼル
エンジンに供給することにより主燃料の燃焼性の
向上を図る方法を特願昭58−153147号(特開昭60
−45765号)として提案した。しかしこの方法は、
2種の燃料を必要とし、かつ空気を酸化触媒反応
装置に導入し、気体(空気)と液体(副燃料)を
固体である触媒に接触させなければならず、効率
的な部分酸化反応をさせることが困難なため、ま
た、空気と副燃料について、ある流量比率を維持
しながらそれぞれ流量制御して反応装置に導入し
なければならず設備、制御が複雑になるため、実
用上問題があつた。 However, the inventors of the present application have developed a method for first burning low-quality fuel with good ignitability, by catalytically partially oxidizing an auxiliary fuel mainly composed of saturated hydrocarbons at a low temperature of about 90 to 220 degrees Celsius to produce peroxide-containing fuel. Japanese Patent Application No. 58-153147 (Japanese Unexamined Patent Publication No. 153147/1983) describes a method of improving the combustibility of the main fuel by converting it into a fuel that has been used in combination with the main fuel and supplying it to a diesel engine.
-45765). However, this method
Two types of fuel are required, and air is introduced into the oxidation catalytic reaction device, and the gas (air) and liquid (auxiliary fuel) must be brought into contact with the solid catalyst to perform an efficient partial oxidation reaction. In addition, there were practical problems because air and auxiliary fuel had to be introduced into the reactor by controlling their respective flow rates while maintaining a certain flow rate ratio, making the equipment and control complex. .
発明の目的
本発明は、パーオキサイドが有するセタン価向
上の性質を利用しつつ、しかも燃料貯蔵中でも酸
化劣化の問題を起こすこと無く、低質な燃料油で
も着火性良く、かつ黒煙の発生を制御して燃焼さ
せることができる燃焼性改良方法を提供すること
にある。Purpose of the Invention The present invention utilizes the property of peroxide to improve the cetane number, does not cause the problem of oxidative deterioration even during fuel storage, has good ignitability even with low-quality fuel oil, and controls the generation of black smoke. The object of the present invention is to provide a method for improving combustibility, which allows combustion to be carried out in a controlled manner.
発明の構成
すなわち本発明の第1は、デイーゼルエンジン
へ液体燃料を供給する際に、該液体燃料にまず酸
素含有気体を加圧溶解させ、次いでこれを酸化触
媒に接触させて該燃料中にパーオキサイドを生成
させ、次いでこれをエンジン燃焼室内に噴射して
燃焼させることからなるデイーゼルエンジン燃料
の燃焼性改良方法である。また本発明の第2は、
前記の酸素含有気体を加圧溶解させた燃料の一部
分を、酸化触媒に接触させることによりパーオキ
サイドを含有する液体燃料とし、これを残余の酸
素含有気体を加圧溶解させた燃料と混合し、これ
をエンジン燃焼室内に噴射して燃焼させることか
らなるデイーゼルエンジン燃料の燃焼性改良方法
である。Structure of the Invention In other words, the first aspect of the present invention is that when supplying liquid fuel to a diesel engine, an oxygen-containing gas is first dissolved in the liquid fuel under pressure, and then the oxygen-containing gas is brought into contact with an oxidation catalyst to form particulate matter in the fuel. This is a method for improving the combustibility of diesel engine fuel, which comprises generating oxide and then injecting it into an engine combustion chamber and combusting it. The second aspect of the present invention is
A portion of the fuel in which the oxygen-containing gas is dissolved under pressure is made into a liquid fuel containing peroxide by contacting with an oxidation catalyst, and this is mixed with a fuel in which the remaining oxygen-containing gas is dissolved under pressure, This is a method for improving the combustibility of diesel engine fuel, which involves injecting this fuel into an engine combustion chamber and combusting it.
作 用
本願の第1の発明は、液体燃料に酸素含有気体
を予め溶解させておき、これを酸化触媒と接触さ
せるため、溶解酸素と燃料が液相で触媒に接触
し、部分酸化反応が効率的に進むとともにそれに
より生成するパーオキサイドの作用により、セタ
ン価の低い燃料でも着火性良く燃焼させることが
できる。更に、燃料噴射時において、部分酸化で
消費されなかつた残存溶解酸素含有気体の作用で
燃料液滴が再微粒化され、排ガス中の黒煙発生が
抑制される。また、第2の発明は、第1の発明と
同様に燃料の着火性を向上させ、排ガス中の黒煙
発生を抑制することができるとともに、パーオキ
サイドを含有した燃料と残余の酸素含有気体を溶
解した燃料とを混合するとき、その混合割合を調
整してエンジン供給燃料中のパーオキサイド生成
量と溶解酸素量を自由に調整できるため、運転条
件の変動に対応し易くなり、排ガス中の黒煙の発
生を一層制御させることができる。しかも、これ
ら発明では、パーオキサイドはエンジン運転中に
生成させ、直ちに燃焼に供するため、燃料劣化へ
の影響はない。Effects In the first invention of the present application, an oxygen-containing gas is dissolved in liquid fuel in advance and brought into contact with an oxidation catalyst, so that the dissolved oxygen and fuel come into contact with the catalyst in the liquid phase, and the partial oxidation reaction is carried out efficiently. Due to the action of the peroxide produced as a result of this progress, even fuel with a low cetane number can be combusted with good ignitability. Furthermore, during fuel injection, the fuel droplets are re-atomized by the action of the residual dissolved oxygen-containing gas that has not been consumed by partial oxidation, thereby suppressing the generation of black smoke in the exhaust gas. In addition, the second invention improves the ignitability of the fuel and suppresses the generation of black smoke in exhaust gas, as in the first invention, and also makes it possible to combust the fuel containing peroxide and the remaining oxygen-containing gas. When mixing with dissolved fuel, the mixing ratio can be adjusted to freely adjust the amount of peroxide produced and the amount of dissolved oxygen in the fuel supplied to the engine, making it easier to respond to fluctuations in operating conditions and reducing the amount of black in exhaust gas. Smoke generation can be further controlled. Moreover, in these inventions, peroxide is generated during engine operation and is immediately subjected to combustion, so it has no effect on fuel deterioration.
実施例
本発明は、デイーゼルエンジンの燃料タンク中
の液体燃料をエンジンの燃焼室へ供給する工程に
適用されるものであつて、エンジンが作動するに
必要な燃料を以下に延べる手段で処理しながら、
エンジンに供給し、これを燃焼させるものであ
る。Embodiments The present invention is applied to the process of supplying liquid fuel in the fuel tank of a diesel engine to the combustion chamber of the engine, and the fuel necessary for the engine to operate is processed by the following means. While
It is supplied to the engine and combusted.
以下本発明を、第1図に基づいてより詳しく説
明する。第1図において、燃料タンク1に貯えら
れた液体燃料2はポンプ3で加圧容器5に送ら
れ、一方圧縮機4で加圧された空気(酸素含有気
体)6は、加圧容器5内で加圧空気の相を形成す
る。該容器内で液体燃料2中に空気を加圧溶解さ
せる。空気が加圧溶解された酸素加圧溶解燃料7
は、配管8の分岐部の三方弁16で二分され、そ
の一部分が酸化触媒14が充填された反応器13
に配管8で導かれ、触媒と充分に接触される。こ
こで溶解酸素を酸化剤として、パーオキサイドが
生成する程度の部分酸化が行われる。次いで、部
分酸化された燃料は、残余の酸素加圧溶解燃料1
5と混合され、燃料ポンプ9で加圧され、燃焼室
11内に燃料噴射ノズル10から噴射される。噴
射により生成した燃料液滴の中の溶解気体は、燃
焼室11内で急速に滴外へ膨張し、その力で液滴
は再微粒化されるためエンジン吸入空気との接触
効率が向上し、また液滴より放出される酸素も燃
焼用酸素として使われ、更に燃料中のパーオキサ
イドの作用と相俟つて着火性が向上し、黒煙の発
生が抑制される。これらの総合作用により効率的
な燃焼を行わせることができる。 The present invention will be explained in more detail below based on FIG. In FIG. 1, liquid fuel 2 stored in a fuel tank 1 is sent to a pressurized container 5 by a pump 3, while air (oxygen-containing gas) 6 pressurized by a compressor 4 is fed into the pressurized container 5. to form a phase of pressurized air. Air is dissolved in the liquid fuel 2 under pressure in the container. Oxygen pressurized dissolved fuel 7 in which air is pressurized and dissolved
is divided into two parts by a three-way valve 16 at a branch part of the pipe 8, and a part thereof is a reactor 13 filled with an oxidation catalyst 14.
is guided through piping 8 to make sufficient contact with the catalyst. Here, partial oxidation is performed using dissolved oxygen as an oxidizing agent to the extent that peroxide is produced. The partially oxidized fuel is then dissolved in the remaining oxygen pressurized dissolved fuel 1
5, is pressurized by a fuel pump 9, and is injected into a combustion chamber 11 from a fuel injection nozzle 10. The dissolved gas in the fuel droplets generated by injection rapidly expands outside the droplets within the combustion chamber 11, and the droplets are re-atomized by this force, improving the efficiency of contact with the engine intake air. In addition, the oxygen released from the droplets is also used as combustion oxygen, which, together with the action of peroxide in the fuel, improves ignitability and suppresses the generation of black smoke. These comprehensive effects enable efficient combustion.
本発明で使用する液体燃料は、軽油又は重油で
あつて、車両用等の高速型デイーゼルエンジン、
小型乃至大型船舶、陸上発電用等の中速乃至低速
型デイーゼルエンジンに広く使用されるものであ
る。即ち軽油は原油の常圧蒸留による直留系の沸
点範囲250〜380℃に大部分の留分を有する留出油
の他、重油等の接触分解や熱分解により生成する
芳香族又は不飽和炭化水素成分を多重に含有する
分解油、ナフサクラツキング時に副生する軽油留
分等、あるいはこれらの水素化処理物が該当す
る。 The liquid fuel used in the present invention is light oil or heavy oil, and is used in high-speed diesel engines for vehicles, etc.
It is widely used in medium- to low-speed diesel engines for small to large ships, land-based power generation, etc. In other words, light oil is distillate oil, which has most of its fraction in the boiling point range of 250 to 380°C, which is obtained by straight-run distillation of crude oil at atmospheric pressure, as well as aromatic or unsaturated carbonized oil produced by catalytic cracking or thermal cracking of heavy oil, etc. This includes cracked oil containing multiple hydrogen components, light oil fractions produced as by-products during naphtha cracking, and hydrogenated products of these.
本発明においては、まず燃料タンクからエンジ
ンの運転に必要な量の液体燃料を連続的に取り出
し、これを加圧した酸素含有気体と接触し、燃料
に酸素を加圧溶解させる。該酸素含有気体には、
窒素等の成分が含有されていても良いため、実用
上空気が好ましく使用される。酸素含有気体を液
体燃料に加圧溶解させるには、液体燃料を耐圧容
器に導入して、これに酸素含有気体を接触させる
など公知の手段が適用できる。 In the present invention, first, an amount of liquid fuel necessary for engine operation is continuously taken out from a fuel tank, and this is brought into contact with pressurized oxygen-containing gas to dissolve oxygen into the fuel under pressure. The oxygen-containing gas includes
Air is preferably used in practice because it may contain components such as nitrogen. In order to dissolve the oxygen-containing gas into the liquid fuel under pressure, known means can be applied, such as introducing the liquid fuel into a pressure-resistant container and bringing the oxygen-containing gas into contact with the container.
液体燃料中へ溶解させる酸素の量は、後述のと
おり部分酸化してパーオキサイド価約300〜
5000ppmを有する燃料を得るために、あるいは更
に燃料噴射時に液滴の再微粒化を促進するために
必要な酸素量とすれば良く、具体的には燃料1
当たりおよそ300〜5000c.c.(標準状態換算)に設
定すれば良い。したがつて加圧溶解する際の酸素
含有気体の圧力は、酸素分圧を3〜20Kgf/cm2
(ゲージ)、また空気を用いる場合、全圧を約15〜
80Kgf/cm2(ゲージ)に設定すれば良い。因に
W.L.Nelson著「Petrolenm Refinery
Engineering」第4版(発行元マグロウヒル)の
第204項、表5−7によると、25℃において、酸
素は軽油1中に酸素分圧760,1560,3800mmHg
でそれぞれ154,380,770c.c.(標準状態)溶解す
る。これらはそれぞれおよそ270,650,1330重量
ppmに相当する。空気を酸素含有気体として用い
る場合、同伴する窒素も溶解するが、これは本発
明において液滴の微粒化に有効に作用する。 The amount of oxygen dissolved in the liquid fuel is partially oxidized as described below to a peroxide value of approximately 300~
The amount of oxygen may be set to the amount necessary to obtain a fuel having 5000 ppm or further to promote re-atomization of droplets during fuel injection.
It should be set to about 300 to 5000c.c. (converted to standard conditions). Therefore, the pressure of the oxygen-containing gas during pressurized dissolution is 3 to 20 Kgf/cm 2 (oxygen partial pressure).
(gauge), or when using air, the total pressure should be approximately 15~
Just set it to 80Kgf/cm 2 (gauge). By the way
“Petrolenm Refinery” by W.L.Nelson
According to Section 204, Table 5-7 of ``Engineering'' 4th edition (published by McGraw-Hill), at 25℃, the oxygen partial pressure in 1 part of diesel oil is 760, 1560, 3800 mmHg.
Dissolve at 154, 380, and 770 c.c. (standard condition), respectively. These weigh approximately 270, 650, and 1330 respectively
Equivalent to ppm. When air is used as the oxygen-containing gas, the entrained nitrogen is also dissolved, which effectively works to atomize the droplets in the present invention.
次いで、前記酸素を加圧溶解した液体燃料(以
下酸素加圧溶解燃料という)の全量もしくは一部
分を、酸化触媒と接触させて、該燃料中の溶解酸
素を酸化剤として該燃料を部分酸化して、燃料中
にパーオキサイドを生成させる。ここで酸素加圧
溶解燃料の全量とは、エンジンの運転に必要な燃
料の量をいい、一方燃料の一部分とは、全量に対
する一部分を意味し、実用的には10〜90wt%の
範囲から選択される。 Next, all or a portion of the liquid fuel in which oxygen is dissolved under pressure (hereinafter referred to as oxygen pressurized dissolved fuel) is brought into contact with an oxidation catalyst to partially oxidize the fuel using the dissolved oxygen in the fuel as an oxidizing agent. , producing peroxide in the fuel. Here, the total amount of oxygen-pressurized dissolved fuel refers to the amount of fuel required for engine operation, while a portion of the fuel refers to a portion of the total amount, and is practically selected from the range of 10 to 90 wt%. be done.
本発明でいう部分酸化とは、パーオキサイドが
生成する程度の酸化を意味し、一酸化炭素、水
素、あるいはメタノールを形成するような改質を
伴う酸化では無い。本発明では、部分酸化によつ
て燃料の炭化水素RH(Rはアルキル基、芳香族
炭化水素基、ナフテン系炭化水素基のいずれか
を、Hは水素を意味する)は、ROOHで表され
るパーオキサイドに変換され、これを含有する液
体燃料になる。液体燃料の部分酸化で生成するパ
ーオキサイドの量は、燃料重量に対する存在する
パーオキサイドが含有する酸素の重量ppm(以下
単にppmで表わす)で表され、これをパーオキサ
イド価(過酸化物価)という。この値はヨウ化カ
リウムを添加して遊離したヨウ素をチオ硫酸ナト
リウムで滴定するASTM D3703「Standard Test
Method for Peroxide Nnmber of Aviation
Tnrbine Fnels(航空タービン燃料のパーオキサ
イド価の標準試験方法)」で求めることができる。
本発明では燃料中のパーオキサイド価が約300〜
5000ppm、好ましくは500〜5000ppmになるよう
部分酸化するのが着火性向上のために好ましい。 Partial oxidation in the present invention means oxidation to the extent that peroxide is produced, and is not oxidation accompanied by modification to form carbon monoxide, hydrogen, or methanol. In the present invention, the hydrocarbon RH (R means any of an alkyl group, an aromatic hydrocarbon group, or a naphthenic hydrocarbon group, and H means hydrogen) of the fuel is expressed as ROOH by partial oxidation. It is converted to peroxide and becomes a liquid fuel containing it. The amount of peroxide produced by partial oxidation of liquid fuel is expressed as the weight of oxygen contained in the peroxide in ppm (hereinafter simply expressed as ppm) relative to the weight of the fuel, and this is called the peroxide value. . This value is determined by the ASTM D3703 "Standard Test", which involves adding potassium iodide and titrating the liberated iodine with sodium thiosulfate.
Method for Peroxide Number of Aviation
It can be determined using "Tnrbine Fnels" (standard test method for peroxide number of aviation turbine fuel).
In the present invention, the peroxide value in the fuel is approximately 300~
It is preferable to partially oxidize to 5000 ppm, preferably 500 to 5000 ppm, in order to improve ignitability.
さて部分酸化反応を行うには、Ni、Cu、Pt、
Pd、Ag等の金属あるいはその酸化物など公知の
酸化触媒の1種あるいは2種以上を反応器に充填
し、これに前記酸素加圧溶解燃料を連続的に通油
し、前記触媒に接触させる。これにより該燃料中
の溶解酸素によつて部分酸化が進み、パーオキサ
イドが形成される。部分酸化の際の反応温度は約
60〜150℃程度で十分であり、接触は液相で行う
ことが可能である。なお、前記パーオキサイド価
は、温度の他、溶解酸素量、触媒との接触時間、
触媒の種類等を適宜選定することによつて調整す
ることができる。 Now, in order to perform a partial oxidation reaction, Ni, Cu, Pt,
A reactor is filled with one or more known oxidation catalysts such as metals such as Pd and Ag or their oxides, and the oxygen-pressurized dissolved fuel is continuously passed through the reactor and brought into contact with the catalyst. . As a result, partial oxidation progresses due to dissolved oxygen in the fuel, and peroxide is formed. The reaction temperature during partial oxidation is approximately
A temperature of about 60 to 150°C is sufficient, and contact can be carried out in a liquid phase. Note that the peroxide value is determined not only by the temperature but also by the amount of dissolved oxygen, the contact time with the catalyst,
It can be adjusted by appropriately selecting the type of catalyst, etc.
酸化触媒に接触させる酸素加圧溶解燃料には、
パーオキサイド形成に必要な酸素が均一に溶解し
ているため、効率良く部分酸化反応が進み、液体
燃料中にパーオキサイドが生成する。また本願発
明は、酸素供給量を酸素含有気体の圧力で、すな
わち酸素溶解量で制御できるため、パーオキサイ
ド生成反応の制御が容易であり、酸化反応が過剰
に進むことも防止できる。具体例を例示すると、
市販軽油に空気を圧力15Kgf/cm2(ゲージ)で溶
解し、この燃料を加圧状態を保持したままアルミ
ナに担持した酸化ニツケル触媒(平均粒径3mm)
500gを充填した反応器に、毎分30mlの速度で通
油し、温度100℃で接触させるとパーオキサイド
価700ppmの部分酸化した燃料が得られる。パー
オキサイド価は触媒の種類、接触時間、接触温
度、酸素溶解量によつて容易に変化させ得る。な
お一般にパーオキサイドは、燃料中に存在する
と、スラツジ生成の原因になるのであるが、本願
発明では、燃料タンク内の燃料に添加するもので
はなく、また部分酸化反応後の燃料は、連続的に
反応器の外にとりだされ、エンジン燃焼室で直ち
に燃焼されるため、このような問題は起こらな
い。 The oxygen pressurized dissolved fuel that is brought into contact with the oxidation catalyst includes:
Since the oxygen necessary for peroxide formation is uniformly dissolved, the partial oxidation reaction proceeds efficiently and peroxide is produced in the liquid fuel. Further, in the present invention, since the amount of oxygen supplied can be controlled by the pressure of the oxygen-containing gas, that is, by the amount of oxygen dissolved, the peroxide production reaction can be easily controlled and the oxidation reaction can be prevented from proceeding excessively. To give a concrete example,
Nickel oxide catalyst (average particle size 3 mm) is made by dissolving air in commercially available light oil at a pressure of 15 Kgf/cm 2 (gauge) and supporting this fuel on alumina while maintaining the pressurized state.
When oil is passed through a reactor filled with 500 g at a rate of 30 ml per minute and brought into contact at a temperature of 100°C, a partially oxidized fuel with a peroxide value of 700 ppm is obtained. The peroxide value can be easily changed depending on the type of catalyst, contact time, contact temperature, and amount of dissolved oxygen. In general, when peroxide is present in fuel, it causes sludge formation, but in the present invention, it is not added to the fuel in the fuel tank, and the fuel after the partial oxidation reaction is continuously This problem does not occur because the fuel is taken out of the reactor and immediately combusted in the engine combustion chamber.
上述のようにして得られたパーオキサイドを含
有する液体燃料は、そのまま、あるいは部分酸化
に供さなかつた残部の酸素加圧溶解燃料と混合さ
れ、エンジンの噴射ノズルからデイーゼルエンジ
ンの燃焼室内に噴射される。噴射されるパーオキ
サイド含有液体燃料には、未反応の酸素、あるい
はこの他酸化反応に関与しなかつた窒素などの気
体が溶解している。前述のとおり、酸素加圧溶解
燃料は全量あるいは一部分が部分酸化に供せら
れ、部分酸化されたパーオキサイド含有の液体燃
料は、それ自信セタン価が大幅に向上しているた
め、着火性が良好である。前述のとおり、酸素加
圧溶解燃料の一部分を部分酸化させた場合では、
部分酸化されパーオキサイドを含有する燃料と、
残余の酸素加圧溶解燃料とを、加圧状態を維持し
て、およそ10:90〜90:10(wt%)で混合して、
これを燃焼室に供給する。この混合割合の選択に
当たつては、混合した後の燃料中のパーオキサイ
ド価が300ppm以上、好ましくは500〜5000ppmに
なるように条件設定するのがセタン価向上のため
に好ましい。残余の酸素溶解燃料をパーオキサイ
ド含有燃料に混合すると、混合燃料中の酸素溶解
量が高まり、排気ガス中の黒煙発生防止作用をも
たらす。すなわち、この混合油を通常のとおりデ
イーゼルエンジンの燃焼室に噴射し、燃料に供す
るが、エンジン燃焼室内へ噴射された液滴状態の
燃料は、燃焼室内で溶解酸素、あるいはこれと同
伴する窒素などの他の溶解気体の急速な膨脹力に
より、一層微粒化され、溶解酸素の液滴外への放
出による酸素富加、パーオキサイドの存在が相俟
つて、デイーゼル燃料の着火の促進と液滴の再微
粒化による液滴の燃料時間の短縮をもたらし、こ
れによつて、黒煙発生を抑制する。 The peroxide-containing liquid fuel obtained as described above is injected into the combustion chamber of a diesel engine from an injection nozzle of the engine, either as it is or mixed with the remaining oxygen pressurized dissolved fuel that has not been subjected to partial oxidation. be done. Unreacted oxygen or other gases such as nitrogen that do not participate in the oxidation reaction are dissolved in the injected peroxide-containing liquid fuel. As mentioned above, all or part of the oxygen-pressurized dissolved fuel is subjected to partial oxidation, and the partially oxidized peroxide-containing liquid fuel has a significantly improved cetane number, so it has good ignitability. It is. As mentioned above, when a part of the oxygen-pressurized dissolved fuel is partially oxidized,
a partially oxidized fuel containing peroxide;
The remaining oxygen pressurized dissolved fuel is mixed at a ratio of approximately 10:90 to 90:10 (wt%) while maintaining the pressurized state.
This is supplied to the combustion chamber. When selecting this mixing ratio, it is preferable to set conditions such that the peroxide number in the fuel after mixing is 300 ppm or more, preferably 500 to 5000 ppm, in order to improve the cetane number. When the remaining oxygen-dissolved fuel is mixed with the peroxide-containing fuel, the amount of dissolved oxygen in the mixed fuel increases, resulting in the effect of preventing black smoke from occurring in the exhaust gas. That is, this mixed oil is injected into the combustion chamber of a diesel engine as usual and used as fuel, but the fuel in the form of droplets injected into the engine combustion chamber is dissolved in the combustion chamber by dissolved oxygen or accompanying nitrogen, etc. The rapid expansion force of other dissolved gases causes further atomization, the release of dissolved oxygen to the outside of the droplets increases oxygen enrichment, and the presence of peroxide promotes ignition of the diesel fuel and regenerates the droplets. Atomization shortens the fuel time of droplets, thereby suppressing the generation of black smoke.
一方部分酸化した燃料をそのまま燃焼に供する
場合、これに残存する溶解酸素量は、パーオキサ
イド形成に全部または一部分が消費されるため、
概して少なくなつているものの、空気を加圧溶解
した場合、窒素は相当量含まれており、このた
め、エンジンの燃焼室内に噴射された燃料液滴
は、残存溶解している酸素、あるいはこれと一緒
に溶解している窒素などの燃焼室内での急速な膨
脹力により、液滴を一層微粒化し、燃料中のパー
オキサイドと相俟つて着火の促進と迅速燃焼をも
たらす。部分酸化した燃料をそのまま、あるいは
混合して用いる場合、燃料中のパーオキサイド価
が500ppmであれば、セタン価はおよそ5程度向
上する。また液滴が燃えつきるのに要する燃焼時
間tは、燃料液滴の粒径rの2乗に比例する(t
∝r2)から、溶解酸素あるいは他の溶解気体によ
る燃料液滴の再微粒化は、燃料液滴の燃えつきる
時間tを大幅に短縮し、もつて未燃焼のスス(黒
煙)の発生を大幅に減少させる。 On the other hand, when partially oxidized fuel is directly used for combustion, all or part of the remaining dissolved oxygen is consumed in peroxide formation.
Although the amount is generally low, when air is dissolved under pressure, it still contains a significant amount of nitrogen, so the fuel droplets injected into the combustion chamber of the engine are free from residual dissolved oxygen or nitrogen. The rapid expansion force of the dissolved nitrogen in the combustion chamber further atomizes the droplets, which, in combination with the peroxide in the fuel, promotes ignition and rapid combustion. When partially oxidized fuel is used as it is or as a mixture, if the peroxide number in the fuel is 500 ppm, the cetane number will improve by about 5. Furthermore, the combustion time t required for a droplet to burn out is proportional to the square of the particle size r of the fuel droplet (t
∝r 2 ), re-atomization of fuel droplets with dissolved oxygen or other dissolved gases can significantly shorten the burning-out time t of fuel droplets, thereby greatly reducing the generation of unburned soot (black smoke). decrease to
発明の効果
本発明の方法によりセタン価が低いデイーゼル
エンジン燃料でも着火性よく、しかも黒煙発生量
を低下させて燃焼させることができるため、特に
セタン価の低い燃料を使用するデイーゼルエンジ
ンに好ましく適用できる。Effects of the Invention The method of the present invention allows even diesel engine fuel with a low cetane number to be ignited with good ignitability and to be combusted with a reduced amount of black smoke generation, so it is particularly preferably applied to diesel engines that use fuel with a low cetane number. can.
第1図は本発明の実施例の一例であり、部分酸
化された燃料を、残余の酸素加圧溶解燃料と混合
してエンジンに供給して、燃焼させるシステムを
示している。同図中2は液体燃料、6は加圧され
た酸素含有気体(加圧空気)、7は酸素加圧溶解
燃料、13は酸化触媒14が充填されている反応
器、15は残余の酸素加圧溶解燃料、10は燃料
噴射ノズル、11はデイーゼルエンジン燃焼室、
12はデイーゼルエンジンのピストンである。
FIG. 1 is an example of an embodiment of the present invention, and shows a system in which partially oxidized fuel is mixed with residual oxygen-pressurized dissolved fuel and supplied to an engine for combustion. In the figure, 2 is a liquid fuel, 6 is a pressurized oxygen-containing gas (pressurized air), 7 is an oxygen pressurized dissolved fuel, 13 is a reactor filled with an oxidation catalyst 14, and 15 is the remaining oxygen pressurized gas. 10 is a fuel injection nozzle, 11 is a diesel engine combustion chamber,
12 is a piston of a diesel engine.
Claims (1)
ンへ液体燃料を供給する際に、(a)燃料タンクから
取り出された燃料に、酸素含有気体を加圧溶解
し、(b)次いで該酸素加圧溶解燃料を、酸化触媒に
接触させて、該燃料を溶解酸素により部分酸化し
て、燃料中にパーオキサイドを生成させ、(c)次い
でパーオキサイドを含有する燃料を、エンジン燃
焼室内に噴射して燃焼させることからなるデイー
ゼルエンジン燃料の燃料性改良方法。 2 デイーゼルエンジンの燃料タンクからエンジ
ンへ液体燃料を供給する際に、(a)燃料タンクから
取り出された燃料に、酸素含有気体を加圧溶解
し、(b)次いで該酸素加圧溶解燃料の一部分を、酸
化触媒に接触させて、該燃料を溶解酸素により部
分酸化して、燃料中にパーオキサイドを生成さ
せ、(c)次いでパーオキサイドを含有する燃料と、
前記の残余の酸素加圧溶解燃料とを混合し、(d)次
いで該混合した燃料を、エンジン燃焼室内に噴射
して燃焼させることからなるデイーゼルエンジン
燃料の燃焼性改良方法。[Claims] 1. When supplying liquid fuel from the fuel tank of a diesel engine to the engine, (a) an oxygen-containing gas is dissolved under pressure in the fuel taken out from the fuel tank, and (b) the oxygen (c) contacting the pressurized dissolved fuel with an oxidation catalyst to partially oxidize the fuel with dissolved oxygen to produce peroxide in the fuel; and (c) injecting the peroxide-containing fuel into the engine combustion chamber. A method for improving the fuel properties of diesel engine fuel, which comprises burning the diesel engine fuel. 2. When supplying liquid fuel from the fuel tank of a diesel engine to the engine, (a) an oxygen-containing gas is dissolved under pressure in the fuel taken out from the fuel tank, and (b) a portion of the oxygen-containing gas is then dissolved under pressure. (c) contacting an oxidation catalyst to partially oxidize the fuel with dissolved oxygen to produce peroxide in the fuel; (c) then a fuel containing peroxide;
A method for improving the combustibility of a diesel engine fuel, which comprises mixing the remaining oxygen pressurized dissolved fuel as described above, and (d) then injecting the mixed fuel into an engine combustion chamber and combusting it.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2438684A JPS60169660A (en) | 1984-02-14 | 1984-02-14 | Combustivity improving method for diesel engine fuel |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2438684A JPS60169660A (en) | 1984-02-14 | 1984-02-14 | Combustivity improving method for diesel engine fuel |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS60169660A JPS60169660A (en) | 1985-09-03 |
| JPH0448938B2 true JPH0448938B2 (en) | 1992-08-10 |
Family
ID=12136732
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2438684A Granted JPS60169660A (en) | 1984-02-14 | 1984-02-14 | Combustivity improving method for diesel engine fuel |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS60169660A (en) |
Families Citing this family (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE19957948C2 (en) * | 1999-12-02 | 2001-11-22 | Geesthacht Gkss Forschung | Method and device for treating fuel |
| CA2324533A1 (en) | 2000-10-27 | 2002-04-27 | Carl Hunter | Oxygen enrichment in diesel engines |
| AU2002241752A1 (en) * | 2000-10-27 | 2002-06-03 | Questair Technologies, Inc. | Feed composition modification for internal combustion engines |
| DE10107616C1 (en) | 2001-02-17 | 2002-10-10 | Daimler Chrysler Ag | Fuel conditioning process |
| JP4519666B2 (en) * | 2005-01-27 | 2010-08-04 | 株式会社デンソー | Fuel supply device |
| US7434568B1 (en) * | 2007-07-03 | 2008-10-14 | Ultimate Combustion Corporation | Method and apparatus for liquid fuel conditioning to improve combustion |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS51127923A (en) * | 1975-04-30 | 1976-11-08 | Nissan Motor Co Ltd | Thermal engine |
| JPS5846177B2 (en) * | 1980-08-13 | 1983-10-14 | 株式会社日立製作所 | semiconductor equipment |
| JPS587820A (en) * | 1981-07-07 | 1983-01-17 | Toshiba Corp | Open-close device for tube inlet in diffusion reactor |
-
1984
- 1984-02-14 JP JP2438684A patent/JPS60169660A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS60169660A (en) | 1985-09-03 |
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