JP4634103B2 - Premixed compression self-ignition and spark ignition combined engine fuel - Google Patents

Description

  The present invention relates to an engine of a type in which the premixed compression self-ignition method and the spark ignition method are switched in accordance with the engine load and the number of revolutions in one engine, and the engine output and the engine rotation region during premixed compression self-ignition combustion with fuel. Premixed compression self-ignition and spark ignition combined engine that can improve the engine thermal efficiency and achieve NOx emission level of 10 mass ppm or less with no catalyst installed and maintain the conventional engine performance during spark ignition combustion Related to fuel.

Today, two types of internal combustion engines for automobiles are widely used: a spark ignition gasoline engine and a compression self-ignition diesel engine.
A spark-ignition gasoline engine is a system in which fuel is injected into an intake port or combustion chamber to form a premixed mixture of fuel and air, and is forcibly ignited and burned by electric discharge by a spark plug. It is required that it is easy to evaporate, difficult to self-ignite, and that the flame propagates smoothly after ignition. In spark-ignition gasoline engines, nitrogen oxides (NOx), hydrocarbons (HC), and carbon monoxide (CO) are exhausted, and three-way catalysts and the like are widely used for purification of these. However, since the exhaust gas purification system using a three-way catalyst can only be applied to a range where the ratio of fuel to air is close to the theoretical air-fuel ratio, there is a disadvantage that the thermal efficiency and fuel consumption are significantly inferior compared with a compression self-ignition diesel engine. is there.

  On the other hand, the compression self-ignition type diesel engine is a system in which the air in the combustion chamber is compressed by the piston rise in the compression process, the temperature rises, and fuel is sprayed and self-ignited and combusted when it reaches the critical temperature of light oil or higher. In addition, fuel characteristics are required to be easily ignited. Although the compression self-ignition type diesel engine is excellent in fuel efficiency and thermal efficiency, the fuel spray is performed from 30 crank angle before compression top dead center to around 10 crank angle after compression top dead center, so the temperature distribution during combustion is shaded, There is a drawback that the amount of NOx and soot emissions is significantly increased. Further, in a compression self-ignition diesel engine, a catalyst for purifying exhaust gas is not so popular, and there is a case where NOx is released into the atmosphere at a very high level of 100 to 1200 mass ppm.

  In this way, the conventional spark ignition gasoline engine can purify the exhaust gas to some extent, but there are problems with fuel efficiency and thermal efficiency, while the compression self-ignition diesel engine has low fuel consumption and high thermal efficiency. There is a problem in terms of exhaust gas such as NOx. For this reason, premixed compression self-ignition engines are currently being studied to solve the problem of simultaneously achieving low NOx emission, low fuel consumption and high thermal efficiency.

A premixed compression self-ignition engine injects fuel into the intake port or the combustion chamber at a fuel injection pressure level of 20 MPa or less, which is significantly lower than the injection pressure in a compression self-ignition diesel engine. This is a system that terminates fuel injection combusted at 60 crank angle before compression top dead center and burns premixed fuel and air by self-ignition rather than forced ignition by a spark plug. A premixed compression self-ignition engine has a longer time from fuel injection to the start of combustion than a conventional compression self-ignition diesel engine, and the fuel is uniformly mixed in the fuel chamber. The high temperature range is not possible, the NOx emission level can be suppressed to 10 ppm or less when no catalyst is installed, and the fuel efficiency and thermal efficiency are as low as those of a compression self-ignition diesel engine. It is possible.
At the current research level, an engine of a type that switches between a premixed compression self-ignition method and a spark ignition method according to the engine load and the engine speed has been developed (for example, see Non-Patent Documents 1 and 2). Development of a dedicated fuel suitable for a new engine is desired.
A. Fuerhapter, “The New AVL CSI Engine-HCCI Operation on a Multi Cylinder Gasoline Engine”, S A・ SAE Technical Paper, 2004-01-0551, 2004 Shiro Yamaoka, “A Study of Controlling the Auto-Ignition and Combustion in a Gasoline HCCI Engine,” SAE Technical Paper ), 2004-01-0942, 2004

  An object of the present invention is an engine of a type in which the premixed compression self-ignition method and the spark ignition method are switched in accordance with the engine load and the rotational speed in one engine. Premixed compression self-ignition method and spark ignition method that expands the rotation range as much as possible, achieves engine thermal efficiency and achieves NOx emission level of 10 mass ppm or less with no catalyst installed, and can maintain conventional engine performance during spark ignition combustion It is to provide a fuel for a combined engine.

  As a result of intensive studies to solve the above problems, the present inventors have found that a fuel having a specific research octane number, a specific composition, and a specific requirement is a premixed compression self-ignition method / spark. The present invention has been completed by finding out that it is suitable as a fuel for an ignition system combined engine.

That is, the present invention has a research octane number of 85 or more and 93 or less, a paraffin content of 60% by volume or more, a total amount of normal pentane, normal hexane and normal heptane of 5% by volume or more, and at least 4 kinds or more. (The isomers are collectively counted as one type), and there are 3 or more types of hydrocarbons containing 2% by volume or more of the total amount of fuel (the isomers are collectively counted as one type), In addition, the present invention relates to a premixed compression self-ignition system / spark ignition system combined engine fuel characterized by satisfying the requirements shown by the following hydrocarbon formula (1).
(1) −66 ≦ −0.66 × normal paraffin content (volume%) − 0.18 × isopara
Fin content (volume%) + 0.16 x olefin content (volume%) + 0.25 x naphthe
(Volume%) + 0.49 × aroma (volume%) ≦ −17.3

The present invention has a density at 15 ℃ is 0.65 g / cm ³ or more 0.78 g / cm ³ or less, an olefin content of 20 vol% or less, initial boiling point 25 ° C. or higher 50 ° C. or less, 50 volume% distillation temperature 70 ° C. or higher and 110 ° C. or lower, 90% by volume distillation temperature is 90 ° C. or higher and 160 ° C. or lower, the end point is 100 ° C. or higher and 210 ° C. or lower, and the lead vapor pressure is 40 kPa or higher and 68 kPa or lower. The present invention relates to a fuel for a combined compression self-ignition method and spark ignition method.

  The fuel of the present invention has a specific research octane number, a specific composition, and a specific requirement. Therefore, the premixed compression self-ignition method and the spark ignition method can be changed with the engine load and rotation in one engine. In the type of engine that switches according to the number, the engine output and the engine rotation range during premixed compression auto-ignition combustion are expanded as much as possible by fuel, improving engine thermal efficiency and achieving NOx emission level of 10 mass ppm or less with no catalyst installed In addition, conventional engine performance can be maintained even during spark ignition combustion. The fuel of the present invention can also be used as a fuel for a hybrid engine that combines a premixed compression self-ignition system / spark ignition system combined engine with an electric motor or the like.

The present invention is described in detail below.
The fuel in the present invention is a fuel suitable for an engine of a type in which the premixed compression self-ignition method and the spark ignition method are switched in accordance with the engine load and the rotational speed in one engine. Here, the premixed compression self-ignition system refers to a combustion mode in which fuel is injected under the following conditions (A), (B), and (C), and combustion is performed by self-ignition.
(A) Fuel injection pressure: 20 MPa or less (B) Fuel injection position: intake port and / or inside combustion chamber (C) Fuel injection end time: 60 crank angle before compression top dead center

In the premixed compression self-ignition method, compared with the compression self-ignition method found in conventional diesel engines, the fuel injection pressure in (A) is remarkably low, and the fuel injection end time in (C), that is, fuel is injected. It takes a long time to start burning. Therefore, in the premixed compression self-ignition method, the fuel is uniformly mixed in the combustion chamber, so that a region having a high temperature locally cannot be formed in the combustion chamber, and the amount of nitrogen oxide emitted is 10 in a state where no catalyst is mounted. It can be made into mass ppm or less.
The premixed compression self-ignition method includes HCCI (Homogeneous Charge Compression Ignition), PCCI (Premixed Charge Compression Ignition), PCI (Premixed Compression Ignition), CAI (Controlled Auto-Ignition), and AR (Active Radical (Combustion)). Sometimes called.
The fuel of the present invention is a fuel suitable for a premixed compression self-ignition type / spark ignition type combined use engine, and a hybrid engine combining the premixed compression self-ignition type / spark ignition type combined use engine and an electric motor or the like. It can also be applied to.

The premixed compression self-ignition system / spark ignition system combined engine fuel (hereinafter also referred to as the fuel of the present invention) of the present invention needs to have a research octane number (RON) of 85 to 93. In order to use a spark ignition engine and a premixed compression self-ignition engine in combination, RON needs to be 85 or more, preferably 87 or more, and more preferably 89 or more. On the other hand, in order to suppress extreme combustion during premixed compression self-ignition combustion, the upper limit needs to be 93 or less, preferably 92 or less, and more preferably 91 or less.
Here, RON is the value of the research octane number measured by JIS K2280 “Petroleum product-fuel oil-octane number test method and cetane number test method and cetane index calculation method”.

The paraffin content of the fuel of the present invention is required to be 60% by volume or more. In order to obtain stable combustion by the premixed compression self-ignition method, it is preferable that the ratio of paraffin constituting the fuel is increased. For this reason, the paraffin content is preferably 75% by volume or more, and more preferably 90% by volume or more.
The paraffin content here is a value measured using a gas chromatograph in accordance with JIS K2536 “Petroleum products-component test method”, and means the total content of isoparaffin content and normal paraffin content. Does not include naphthene.

The fuel of the present invention needs to have a total content of normal pentane, normal hexane and normal heptane of 5% by volume or more. Normal pentane, normal hexane and normal heptane are hydrocarbons with good ignitability, high volatility, and indispensable for improving the operability of HCCI engines, so the total content of these hydrocarbons is 8 volumes. % Or more, preferably 10% by volume or more.
In addition, each content of normal pentane here, normal hexane, and normal heptane is the value measured using a gas chromatograph based on JISK2536 "petroleum product-component test method".

The fuel of the present invention has an important balance between distillation properties and ignitability, and is required to be composed of at least four types of hydrocarbons. However, even if the number of carbon atoms is the same, straight-chain hydrocarbons are straight-chain hydrocarbons counted as one type of hydrocarbon, and branched hydrocarbons are branched-chain hydrocarbons, including each isomer, as one type of hydrocarbon. It shall be counted. For example, as for octane, n-octane is one type, 2,2,4-trimethylpentane, 2,2,3-trimethylpentane, 2,3,4-trimethylpentane, 2,3,3-trimethylpentane. , 2,3-dimethylhexane, 2,4-dimethylhexane, 2,5-dimethylhexane and the like are collectively referred to as isooctane (branched hydrocarbon) and counted as one kind. Therefore, in this case, it counts as two types of hydrocarbons, n-octane and isooctane.
Further, the fuel of the present invention requires that 2% by volume or more of hydrocarbons are present in the fuel in 3 or more types. In this case as well, when the number of carbon atoms is the same as described above, the straight chain hydrocarbon is counted as one type of straight chain hydrocarbon, and the branched hydrocarbon is classified as one type including the isomer as a branched hydrocarbon. It shall be counted.

The fuel of the present invention is “−0.66 × normal paraffin content (volume%) − 0.18 × isoparaffin content (volume%) + 0.16 × olefin content (volume%) + 0.25 × naphthene content (volume%) The parameter represented by the hydrocarbon formula of “+ 0.49 × aroma content (volume%)” needs to be −66 or more and −17.3 or less (however, naphthene is not included in paraffins). ).
The hydrocarbon formula is obtained from a premixed compression self-ignition characteristic test of fuel, and indexes the ease of occurrence of a low-temperature oxidation reaction. Low-temperature oxidation reactions related to the ease of ignition of the premixed compression self-ignition method are likely to occur in the order of normal paraffinic hydrocarbons, isoparaffinic hydrocarbons, olefinic hydrocarbons, naphthenic hydrocarbons, and aromatic hydrocarbons. Naphthenic hydrocarbons and aromatic hydrocarbons are not suitable for HCCI combustion, and are liable to produce benzene and the like during premixed compression self-ignition combustion, which is not preferable in terms of exhaust gas. The value of the hydrocarbon type described above is suitable for small as homogeneous charge compression ignition combustion, good Mashiku -60 or -20 or less, more preferably -40 or -20 or less.
Note that the normal paraffin content (volume%), isoparaffin content (volume%), olefin content (volume%), naphthene content (volume%), and aroma content (volume%) mentioned here are JIS K2536 “Petroleum products-component test”. Each value is measured using a gas chromatograph in accordance with “Method”.

The olefin content in the fuel of the present invention is preferably 20% by volume or less. If the olefin content in the fuel is large, premixed compression self-ignition is hindered and knocking specific to premixed compression self-ignition tends to occur, which is not preferable. The knocking specific to this premixed compression self-ignition is different from the intermittent knocking of gasoline that occurs when the combustion mixture compresses the end gas, and is continuously generated by knocking caused by the combustion of fuel at one time. There are features. Further, the olefin content has an effect of increasing the exhaust gas temperature, which is not preferable from the viewpoint of reducing nitrogen oxides. For this reason, it is more preferably 10% by volume or less.
In addition, the olefin content here is a value measured using a gas chromatograph in accordance with JIS K2536 “Petroleum products—component test method”.

Although there is no restriction | limiting in particular about the density (15 degreeC) of the fuel of this invention, From a viewpoint that an accelerator response becomes dull, it is preferable that it is 0.78 g / cm < ³ > or less, More preferably, it is 0.76 g / cm < ³ > or less. In view of problems such as vapor lock, it is preferably 0.65 g / cm ³ or more, more preferably 0.68 g / cm ³ or more.
In addition, the density here is a value measured by JIS K2249 “Density test method and density / mass / capacity conversion table for crude oil and petroleum products”.

The fuel of the present invention has an initial boiling point (IBP) of 25 ° C. or more and 50 ° C. or less, a 50 volume% distillation temperature (T50) of 70 ° C. or more and 110 ° C. or less, and a 90 volume% distillation temperature (T90) of 90 ° C. or more. It is preferable that it is 160 degrees C or less and an end point (EP) is 100 degreeC or more and 210 degrees C or less.
The IBP is preferably 50 ° C. or less, more preferably 45 ° C. or less, more preferably 40 ° C. or less because the evaporation characteristics of the fuel in the premixed compression self-ignition method deteriorates and it becomes difficult to obtain desired thermal efficiency and fuel consumption. The following is more preferable. On the other hand, it is preferable that IBP is 25 ° C. or higher from the viewpoint of preventing the light gas evaporative gas in the fuel from leaking from the fuel tank and being released into the atmosphere.
The T50 is preferably 110 ° C. or lower, more preferably 100 ° C. or lower, more preferably 90 ° C., in order to prevent the balance with the light fraction from being lost and the thermal efficiency during premixed compression self-ignition combustion to deteriorate. The following is more preferable. On the other hand, the lower limit of T50 is preferably 70 ° C. or higher, and more preferably 75 ° C. or higher, because there is a possibility that the air charging efficiency exerted by the evaporation of the fuel may deteriorate.
T90 is preferably 160 ° C. or lower because it is necessary that the premixed gas is completely vaporized before ignition in both the premixed combustion method and the spark ignition combustion method. ° C or lower is more preferable, and 120 ° C or lower is most preferable. On the other hand, the lower limit is preferably 90 ° C. or higher from the viewpoint of obtaining good fuel efficiency.
When the EP exceeds 210 ° C., the ignition is not stable, and its control becomes difficult, and the maximum output, thermal efficiency, and exhaust gas amount are deteriorated. Therefore, the EP is preferably 210 ° C. or less, more preferably 180 ° C. or less, 160 ° C. or lower is more preferable. On the other hand, the lower limit is preferably 100 ° C. or higher because the maximum output may be lowered.
Here, IBP, T50, T90 and EP are values measured according to JIS K2254 “Petroleum products—Distillation test method—Atmospheric pressure distillation test method”.

The reed vapor pressure (RVP) of the fuel of the present invention is preferably 40 kPa or more and 68 kPa or less. 40 kPa or more and 64 kPa or less are more preferable from the viewpoint of preventing deficiencies in drivability due to vapor lock or the like.
The vapor pressure (RVP) here is a value measured by JIS K 2258 “Crude oil and fuel oil vapor pressure test method (Lead method)”.

In the fuel of the present invention, the content of sulfur is not particularly limited, but is preferably 10 ppm by mass or less. If the amount exceeds 10 ppm by mass, the exhaust gas purification catalyst mounted on the engine is poisoned by sulfur, which causes a problem that the exhaust gas purification capacity is lowered, which is not preferable. The sulfur content in the fuel is more preferably 5 ppm by mass or less, and most preferably 1 ppm by mass or less from the viewpoint of maintaining the performance of the catalyst.
Here, the sulfur content is a value measured according to JIS K2541 “Crude oil and petroleum product one sulfur content test method”.

The fuel of the present invention contains hydrocarbon as a main component, but may contain oxygen-containing compounds such as ether, alcohol, ketone, ester, glycol and the like.
Examples of the oxygen-containing compound include methanol, ethanol, normal propyl alcohol, isopropyl alcohol, normal butyl alcohol, isobutyl alcohol, dimethyl ether, diisopropyl ether, methyl tertiary butyl ether (MTBE), ethyl tertiary butyl ether (ETBE), and tertiary amyl. Examples include methyl ether (TAME) and tertiary amyl ethyl ether.
The fuel of the present invention can reduce the amount of HC in the exhaust gas by containing the oxygen-containing compound, but the amount of NOx increases. Therefore, the content ratio of the oxygen-containing compound is preferably 20% by mass or less, more preferably 10% by mass or less, and most preferably 3% by mass or less with respect to the total amount of fuel in terms of oxygen element (oxygen content).

  The base material of the fuel of the present invention is not particularly limited as long as a fuel having a predetermined property can be obtained as described above. For example, a crude oil distillation device, a naphtha reforming device, an alkylation device, etc. From propane, mainly from propane, straight butane from butane, straight desulfurized propane, desulfurized butane, and catalytic cracking equipment Cracked propane fractions mainly from propane / propylene, cracked butane fractions centered on butane / butene, naphtha fractions obtained by atmospheric distillation of crude oil (full-range naphtha), light naphtha Distillate (light naphtha), heavy fraction of naphtha (heavy naphtha), desulfurized full range naphtha desulfurized full range naphtha, desulfurized light naphtha desulfurized light naphtha, dehydrated heavy naphtha Desulfurized heavy naphtha, light naphtha converted to isoparaffins by isomerization equipment, alkylates obtained by adding (alkylating) lower olefins to hydrocarbon compounds such as isomerized gasoline and isobutane, catalytic reforming Reformed gasoline obtained by the method, raffinate, which is a residue of aromatics extracted from reformed gasoline, light fraction of reformed gasoline, medium heavy fraction of reformed gasoline, heavy fraction of reformed gasoline , Cracked gasoline obtained by catalytic cracking method, hydrocracking method, etc., light fraction of cracked gasoline, heavy fraction of cracked gasoline, natural gas, etc. are decomposed into carbon monoxide and hydrogen and then FT ( It can be prepared by mixing one kind or two or more kinds of base materials such as a light fraction of GTL (Gas to liquids) obtained by Fischer-Tropsch synthesis.

In the fuel of the present invention, if necessary, an appropriate amount of a wear modifier can be blended to improve the lubricity of the resulting fuel. Examples of main wear control agents include higher alcohols; alcohol compounds having 1 to 4 hydroxyl groups and 1 to 30 carbon atoms; higher carboxylic acids; reaction products of higher monocarboxylic acids and glycols or trihydric alcohols. A hydroxyl group-containing ester; an ester of a higher polycarboxylic acid and a polyhydric alcohol; a composition containing> NR (where R is a hydrocarbon group having 5 to 40 carbon atoms) and having at least one substituent. Examples include esters of polyhydric alcohols combined with one nitrogen compound; amide compounds of higher carboxylic acids and alcohol amines, and the like. These can be used alone or as a mixture.
Among these, a hydroxyl group-containing ester which is a reaction product of a higher monocarboxylic acid having 10 to 25 carbon atoms and glycol or a trihydric alcohol and / or an amide of a higher carboxylic acid having 5 to 25 carbon atoms and an alcohol amine. A compound is preferable, and an amide compound of a higher monocarboxylic acid having 10 to 25 carbon atoms and glycerin ester and / or a higher monocarboxylic acid having 5 to 25 carbon atoms and diethanolamine is most preferable.
The amount of addition of the wear modifier is not particularly limited, but it is usually per liter of fuel of the present invention in that sufficient fuel consumption and output improvement effect can be exhibited, while improvement cannot be expected even if added more than that. It is preferable to add so that it may become a content rate of 10-300 mg, Preferably 30-250 mg.
In addition, in the case of products that are marketed as wear modifiers, the active ingredients that contribute to wear resistance may be diluted with a suitable solvent, so when such commercial products are added to the fuel of the present invention. Means the addition amount as an active ingredient.

(Other additives)
The fuel of the present invention may contain other fuel oil additives other than the wear modifier and the like as necessary. Other fuel oil additives include, for example, detergent dispersants such as succinimide, polyalkylamine and polyetheramine, N, N′-diisopropyl-p-phenylenediamine, N, N′-diisobutyl-p-phenylene Antioxidants such as diamines, 2,6-di-t-butyl-4-methylphenol, hindered phenols, etc .; metal impurities such as amine carbonyl condensation compounds such as N, N′-disalicylidene-1,2-diaminopropane Activators, surface ignition inhibitors such as organic phosphorus compounds, antifreezing agents such as polyhydric alcohols and ethers thereof, alkali metal or alkaline earth metal salts of organic acids, auxiliary alcohols such as higher alcohol sulfates, anions Surfactants, cationic surfactants, amphoteric surfactants and other antistatic agents, azo dyes and other colorants, organic carboxylic acids and the like Derivatives, rust inhibitors such as alkenyl succinic acid esters, draining agents such as sorbitan esters, quinizarin, odorants such as identification agent coumarin, and the like. These additives can be added singly or as a mixture, and it is preferable to add them in such a ratio that the total amount of these additives is 0.1% by mass or less based on the total amount of fuel. Here, the total amount of additive means the amount added as an active ingredient of the additive.

  EXAMPLES The present invention will be specifically described below with reference to examples and comparative examples, but the present invention is not limited to these examples.

(Examples 1-5 and Comparative Examples 1-2)
According to the composition shown in Table 1, fuels of the present invention (Examples 1 to 5) and comparative fuels (Comparative Examples 1 and 2) were prepared by a conventional method. Table 2 shows the hydrocarbon compound content of each fuel obtained, and the measurement results of distillation properties, density, and sulfur content.
The obtained fuel was evaluated by performing the following tests using the following premixed compression self-ignition engine. The results are shown in Table 3.

(Engine specifications)
Engine type: Inline 6-cylinder premixed compression self-ignition engine Displacement: 2000cc
Compression ratio: 14
Fuel injection pressure: 8MPa

(Engine test)
<Case 1> ... Comparison of driving performance in the premixed compression self-ignition method The engine is operated according to the following procedure, a rotation-output curve diagram (map) is created, and the maximum operable speed, maximum torque, nitrogen The oxide amount and engine start time were determined.
(1) A dynamometer (DC95: 220 kW DC dynamometer manufactured by Meidensha) is set to rotation-intake pressure control, and the engine is motored at a predetermined rotation speed.
(2) Inject fuel and gradually increase the injection amount.
(3) When self-ignition combustion is started, the output corresponding to the fuel injection amount, the fuel consumption amount, the exhaust gas, and the knocking level are measured.
(4) The fuel injection amount is increased until operation is impossible, and the operation (3) is continued.
(5) Repeat (2) to (4) while changing the rotation speed.

  Nitrogen oxide emissions were measured with an exhaust gas analyzer (MEXA9100 manufactured by Horiba, Ltd.) by sampling combustion exhaust gas from the engine exhaust pipe at each maximum torque at an engine speed of 1000 rpm.

(Engine start time)
The engine is allowed to cool for 48 hours at -15 ° C., and then the starter is started, and then the first cylinder is first exploded (the premixed gas in the cylinder is ignited for the first time after the starter is started). I measured the time required to do. The longer this time, the worse the engine startability.

  From the results of Table 3, it can be seen that when the fuel of the present invention (Examples 1 to 5) is used, the maximum torque and the maximum rotation speed can be increased as compared with the fuels of Comparative Examples 1 and 2. Further, it can be seen that the amount of nitrogen oxide emission can be reduced and the engine start time can be shortened.

<Case 2> ... Comparison of driving performance with spark ignition method At each engine speed of 3000 rpm, 4000 rpm and 5000 rpm, a throttle fully open (WOT) output performance test was performed and the maximum output at each speed was compared ( Unit is horsepower).
Furthermore, a traveling load was applied to the dynamometer, an acceleration test was performed from an engine speed of 3000 rpm to 5000 rpm, and a time until reaching 3000 rpm to 5000 rpm was measured.
From the results in Table 3, it can be seen that when the fuel of the present invention (Examples 1 to 5) is used, the maximum output and acceleration time are equivalent or better than those of Comparative Examples 1 and 2. .

Claims (2)

The research octane number is 85 or more and 93 or less, the paraffin content is 60% by volume or more, the total amount of normal pentane, normal hexane and normal heptane is 5% by volume or more, and at least four kinds of hydrocarbons (isomers) Is counted as one type), there are 3 or more types of hydrocarbons containing 2% by volume or more of the total fuel (isomers are counted as one type collectively), and the following hydrocarbon formula ( A fuel for a premixed compression self-ignition method / spark ignition method combined engine characterized by satisfying the requirements shown in 1).
(1) −66 ≦ −0.66 × normal paraffin content (volume%) − 0.18 × isopara
Fin content (volume%) + 0.16 x olefin content (volume%) + 0.25 x naphthe
(Volume%) + 0.49 × aroma (volume%) ≦ −17.3 15 Density at ° C. is 0.65 g / cm ³ or more 0.78 g / cm ³ or less, an olefin content of 20 vol% or less, initial boiling point 25 ° C. or higher 50 ° C. or less, 50% by volume distillation temperature of 70 ° C. to 110 2. The premixed compression self according to claim 1, wherein 90% by volume distillation temperature is 90 ° C. or higher and 160 ° C. or lower, the end point is 100 ° C. or higher and 210 ° C. or lower, and the reed vapor pressure is 40 kPa or higher and 68 kPa or lower. Ignition and spark ignition combined engine fuel.