JP4926513B2 - Fuel oil composition for compression self-ignition engine - Google Patents

Description

  The present invention relates to a fuel oil composition for a compression self-ignition engine, and more particularly to a fuel oil composition capable of achieving premixed compression self-ignition combustion with excellent exhaust gas characteristics and low combustion noise.

In recent years, reduction of exhaust gas emitted from automobiles and improvement of thermal efficiency have been demanded due to environmental problems. Diesel engines have higher thermal efficiency than gasoline engines, and have low carbon dioxide (CO ₂ ) emissions, which are said to be related to global warming. However, in a diesel engine based on normal diffusion combustion, smoke and nitrogen oxide (NOx) emissions are problematic due to the fact that the fuel concentration is partly too high and a high temperature combustion region is formed. As a new technique for solving this problem, a premixed compression self-ignition engine has attracted attention (for example, see Non-Patent Document 1).

  The premixed compression self-ignition combustion performed in the above premixed compression self-ignition engine is a phenomenon in which fuel is self-ignited and burned when the fuel and air are compressed in a lean premixed state. However, it is possible to simultaneously reduce NOx and smoke in the exhaust gas by forming a lean premixed gas by adjusting the fuel injection timing by injecting the fuel at an early stage and igniting it with compression. However, in general, when premixed compression ignition combustion is applied under high load conditions, not only the exhaust gas but also the combustion noise may increase due to the deterioration of the mixture formation and the rapid combustion mode. Auto-ignition combustion is limited to areas with relatively low loads. Therefore, since the operation in the high load region requires the operation of performing normal diffusion combustion by changing the fuel injection timing, even in the premixed compression self-ignition engine, the fuel injection nozzle ( Hole nozzle) and combustion chamber shape are required. Here, in a normal diesel engine using a hole nozzle, when operating by premixed compression self-ignition combustion by early injection using general light oil, it depends on diffusion combustion using conventional general light oil Compared to the operation by diesel combustion, the generation of NOx and smoke is suppressed, and the exhaust gas has excellent characteristics with a small content of these, but the suppression of the generation of NOx and smoke is still not satisfactory. In addition, it has been difficult to achieve premixed compression self-ignition combustion exhibiting sufficiently excellent operation characteristics such as causing combustion noise.

  In premixed compression self-ignition combustion, fuel is injected into the engine cylinder and then premixed with air. The fuel oxidation reaction proceeds sequentially and undergoes a process of ignition and combustion. Qi formation and ignition timing are important points, and the physical and chemical characteristics of the fuel itself are greatly affected. Therefore, depending on the nature of the fuel, it is considered that premixed compression self-ignition combustion may be achieved even in a normal hole nozzle or combustion chamber-shaped diesel engine. Based on this idea, a fuel oil composition for a premixed compression self-ignition engine that enables premixed compression ignition combustion with less exhaust gas by controlling the distillation property and cetane number of the fuel composition has been proposed (patent) Reference 1). However, this fuel oil composition has not yet solved the problems related to combustion noise described above, and further improves the quality of the fuel used for premixed compression self-ignition combustion, resulting in low exhaust gas characteristics and low combustion noise characteristics. It is demanded to make it compatible.

JP 2004-315604 A Rudolf H.R. Stanglemaier and Charles E.M. Roberts, SAE Paper NO. 1999-01-3682

  The present invention has been made in view of the above-described conventional situation, paying attention to the magnitude of the influence of the properties of fuel in premixed compression self-ignition combustion, and the relationship between premixed compression self-ignition combustion and fuel properties. It is an object of the present invention to provide a fuel oil composition that can be fully investigated and can exhibit premixed compression self-ignition combustion with sufficiently excellent exhaust gas characteristics and low combustion noise.

  Therefore, as a result of intensive studies to achieve the above object, the present inventors have adjusted the cetane number for each constant boiling fraction to a specific range, and set the cetane number of the entire fuel to be within a certain range. This makes it possible to reduce combustion noise when performing premixed compression ignition combustion with low exhaust gas concentration by early injection, exhibiting sufficiently excellent exhaust gas characteristics, and premixed compression with low combustion noise It has been found that a fuel oil composition capable of achieving self-ignition combustion can be prepared, and the present invention has been completed.

That is, this invention provides the following fuel oil composition for compression self-ignition engines, in order to achieve the said objective.
(1) The initial boiling point is 20 ° C to 135 ° C, the 50% distillation point is 60 ° C to 250 ° C, the end point is 200 ° C to 350 ° C, and the kinematic viscosity at 30 ° C is 0.4 mm ² / s. The cetane number of the fraction having a boiling point of less than 150 ° C. is 10 or more and 45 or less, and is 3.0 mm ² / s or less, the sulfur content is 10 mass ppm or less, the cetane number of the whole fuel is 30 or more and 50 or less. , and the boiling point of 0.99 ° C. or more distillate cetane number Ri der 30 or more 95 or less, and a fraction of the cetane number having a boiling point of less than 150 ℃ (150-CN) and a boiling point fraction above 0.99 ° C. A fuel oil composition for a compression self-ignition engine, wherein the ratio of cetane number (150 + CN) [(150-CN) / (150 + CN)] is 1 or less .
( 2 ) End point is 200 degreeC or more and 300 degrees C or less, The fuel oil composition for compression self-ignition engines as described in said ( 1 ) characterized by the above-mentioned.

  ADVANTAGE OF THE INVENTION According to this invention, the fuel oil composition which can achieve the premixing compression self-ignition combustion which shows the exhaust gas characteristic which was fully excellent, and shows low combustion noise is provided.

Hereinafter, the present invention will be described in detail.
The fuel oil composition of the present invention includes a naphtha fraction obtained by atmospheric distillation of crude oil, a desulfurized naphtha obtained by desulfurizing the naphtha fraction, a reformed gasoline obtained by catalytic reforming of the desulfurized naphtha, and a modified gasoline. Debenzene-modified gasoline with benzene removed from high-quality gasoline, kerosene fraction obtained by atmospheric distillation of crude oil, desulfurized kerosene obtained by desulfurizing kerosene fraction, and catalytic cracking and hydrogenation of heavy oil Gasoline, kerosene fraction obtained by cracking or pyrolysis, alkylate produced from olefin and isobutane, isomerized isomerate, hydrocarbon with 4 or 5 carbon atoms, etc. Can be appropriately blended and prepared. In addition, paraffinic hydrocarbons and alcohol fuels by Fischer-Tropsch synthesis, paraffinic solvents having various carbon numbers, naphthenic solvents, aromatic solvents, and the like can also be used as raw materials. Further, the fuel oil composition of the present invention can be suitably adjusted by appropriately blending various raw material fractions as described above, but if necessary, obtained as a direct fraction from crude oil. Is also possible.

  In the fuel oil composition of the present invention, the sulfur content is 10 mass ppm or less, preferably 8 mass ppm or less. When the sulfur content is more than 10 mass ppm, the content of sulfur oxide in the exhaust gas may increase, and the catalyst for treating the exhaust gas may be poisoned. The sulfur content can be measured by the microcoulometric titration method of JIS K2541.

The fuel oil composition of the present invention, the initial boiling point equal to or less than 135 ° C. 2 0 ° C. or more, good Mashiku is 100 ° C. or less 20 ° C. or higher. When the initial boiling point is higher than 135 ° C., the volatility of the fuel oil composition becomes poor. Therefore, the mixing ratio of the fuel oil composition and air decreases, so when performing premixed compression self-ignition combustion, smoke or carbonization is performed. A lot of hydrogen may be discharged. When the initial boiling point is lower than 20 ° C., a large amount of vapor of the fuel oil composition is generated in the fuel pump or the fuel pipe, which may hinder the distribution of the fuel oil composition.

The fuel oil composition of the present invention, 50% distillation point or less 250 ° C. 6 0 ° C. or higher, good Mashiku is at 80 ° C. or higher 230 ° C. or less, more preferably at 100 ° C. or higher 200 ° C. or less . When the 50% distillation point is higher than 250 ° C., the volatility of the fuel becomes poor. Therefore, the mixing ratio of the fuel oil composition and air decreases, so when performing premixed compression self-ignition combustion, smoke and hydrocarbons are used. May be discharged. When the 50% distillation point is lower than 60 ° C., a large amount of vapor of the fuel oil composition is generated in the fuel pump or the fuel pipe, which may hinder the distribution of the fuel oil composition.

The fuel oil composition of the present invention, the endpoint is not more than 350 ° C. 2 00 ° C. or more, good Mashiku is 200 ° C. or higher 300 ° C. or less. When the end point is higher than 350 ° C., the volatility of the fuel oil composition becomes poor, and therefore, the mixing ratio of the fuel oil composition and air decreases, so when performing premixed compression self-ignition combustion, smoke and hydrocarbons are not generated. A lot may be discharged. When the end point is lower than 200 ° C., the fuel oil composition vapor may be generated in a large amount in the fuel pump or the fuel pipe at a high temperature such as in summer, and the distribution of the fuel oil composition may be hindered. The distillation range is extremely narrow, so that the yield is too low to be efficient.
The distillation properties such as the initial boiling point, 50% distillation point, and end point can be measured by the atmospheric pressure method of the petroleum product distillation test method of JIS K 2254.

In the fuel oil composition of the present invention, the kinematic viscosity at 30 ° C. is 0 . A less 4 mm ² / s or more 3.0 mm ² / s, good Mashiku is less 0.4 mm ² / s or more 2.5 mm ² / s, more preferably 0.5 mm ² / s or more 2.0mm ² / s or less. If the kinematic viscosity is higher than 3.0 mm ² / s, the spray angle of the fuel oil composition becomes narrow and the atomization is hardly promoted, so that the formation of the premixed gas becomes worse. If the kinematic viscosity is too low, the fuel pump or the like may be worn, which is not preferable. The kinematic viscosity can be measured by a petroleum product kinematic viscosity test method of JIS K2283.

  In the fuel oil composition of the present invention, the cetane number is 30 or more and 50 or less, preferably 35 or more and 45 or less. When premixed compression self-ignition combustion is performed, if the cetane number is lower than 30, hydrocarbon emissions may increase. On the other hand, when the cetane number is higher than 50, combustion noise may be high because premixed compression self-ignition combustion may be accompanied by a rapid heat generation when attempting to achieve a higher load.

  In the fuel oil composition of the present invention, the cetane number of the fraction having a boiling point of less than 150 ° C. (hereinafter also referred to as 150-CN) is 10 or more and 45 or less, preferably 10 or more and 40 or less. When premixed compression self-ignition combustion is performed, if the cetane number of the fraction having a boiling point of less than 150 ° C. is lower than 10, the amount of hydrocarbon emissions may increase. On the other hand, if the cetane number of the fraction having a boiling point of less than 150 ° C. is higher than 45, combustion noise may increase when premixed compression ignition combustion is performed.

  In the fuel oil composition of the present invention, the cetane number of a fraction having a boiling point of 150 ° C. or higher (hereinafter also referred to as 150 + CN) is 30 to 95, preferably 35 to 95. In the case of premixed compression self-ignition combustion, if the cetane number of a fraction having a boiling point of 150 ° C. or higher is lower than 35, the amount of hydrocarbon emissions may increase, and combustion noise in premixed compression ignition combustion may increase. May be larger. On the other hand, even if the cetane number of a fraction having a boiling point of 150 ° C. or higher is higher than 95, combustion noise may increase.

In the fuel oil composition of the present invention, the ratio of the cetane number (150-CN) of the fraction having a boiling point of less than 150 ° C. to the cetane number (150 + CN) of the fraction having a boiling point of 150 ° C. or more [(150-CN) / ( 0.99 + CN)] is 1 or less, good Mashiku is 0.8 or less. If this ratio is 1 or less, it becomes possible to further suppress combustion noise in premixed compression ignition combustion.
The cetane number can be measured by the fuel oil cetane number test method of JIS K 2280. Regarding the cetane number by fractionation, the cetane number of the fuel preparation base material corresponding to each fraction may be measured, or the fuel oil composition of the present invention may be fractionated by distillation, The cetane number may be measured.

  In the fuel oil composition of the present invention, known fuel additives such as antioxidants, anti-icing agents, auxiliary agents, antistatic agents, rust preventives, discriminating agents, colorants, detergents, if necessary, An appropriate amount of a cetane number improver, an antifoaming agent, an antioxidant, a fluidity improver, a lubricity improver and the like can be added.

  Next, the present invention will be described more specifically with reference to examples and comparative examples. In addition, this invention is not restrict | limited at all by these examples.

Examples 1-3 and Comparative Examples 1-5
A fuel oil composition having the properties shown in Table 1 was prepared as described below and evaluated by the following method.
Example 1: 50% by volume of isooctane, 20% by volume of isoparaffin solvent having a boiling point range of 206 to 257 ° C., and 30% by volume of normal paraffin having 14 carbon atoms were mixed.
Example 2: Substrates obtained by hydrodesulfurizing a heavy naphtha fraction (boiling range 80 ° C to 140 ° C) and a kerosene fraction (boiling range 145 ° C to 245 ° C) obtained by atmospheric distillation of crude oil, respectively. Prepared by mixing equal volumes.
Example 3: 43% by volume of heavy reformate having a boiling range of 104 ° C to 177 ° C, 13% by volume of n-paraffin having a boiling range of 70 ° C to 103 ° C, and n-paraffin having a boiling range of 169 ° C to 257 ° C Was prepared by mixing an isoparaffin solvent having a boiling point of 166 ° C. to 266 ° C. in a proportion of 9% by volume.

Comparative Example 1: Prepared by mixing 50% by volume of normal heptane, 45.5% by volume of isoparaffin solvent having a boiling range of 206 to 257 ° C., and 4.5% by volume of normal paraffin having 14 carbon atoms.
Comparative Example 2: 31% by volume of an aromatic solvent having a boiling point range of 161 ° C. to 245 ° C., 2.8% by volume of α-methylnaphthalene, 55% by volume of n-paraffin mixture having a boiling point range of 75 ° C. to 150 ° C., carbon Several 14 n-paraffins were mixed at a ratio of 11.2% by volume.
Comparative Example 3: A kerosene fraction (boiling range: 170 ° C. to 360 ° C.) obtained by atmospheric distillation of crude oil was subjected to hydrodesulfurization, and 47% by volume of an isoparaffin solvent having a boiling range of 200 ° C. to 330 ° C. Prepared by blending.
Comparative Example 4: A kerosene fraction (145 ° C to 245 ° C) obtained by atmospheric distillation of crude oil was mixed with 80% by volume of isoparaffin solvent having a boiling point range of 80 ° C to 240 ° C. Prepared.
Comparative Example 5: A general No. 2 light oil was used.

  As an evaluation test engine, a diesel engine equipped with an in-line 4-cylinder, displacement 2L, common rail fuel injection device, turbocharger with intercooler, and cooled exhaust gas recirculation device was used. Table 2 shows the main specifications of the test engine. In this test engine, premixed compression self-ignition combustion is enabled by setting the compression ratio to 15 and setting the fuel injection timing earlier than in the case of normal diesel combustion.

  Fuel oil compositions prepared in each Example and each Comparative Example using the above test engine under the conditions of engine speed: 2000 rpm, fuel injection pressure: 50 MPa, injection timing: 30 ° top dead center, torque: 60 Nm Combustion noise, hydrocarbon emissions (THC), NOx emissions, smoke emissions (FNS) during premixed compression ignition combustion were measured. Note that NOx, CO, THC and other exhaust gas measurements were made directly from the exhaust pipe with an automobile exhaust gas analyzer. The combustion noise was derived from the in-cylinder pressure waveform using a combustion noise meter. The evaluation results are shown in Table 3.

* 1: Filter Smoke Number: An evaluation method in which a predetermined amount of exhaust gas is sucked through paper and the reflectance of the attached smoke is measured. Evaluation is made with white = 0 and black = 10, and a value between 0 and 10 is evaluated between white and black. That is, by irradiating the measurement paper with light and measuring the reflected light with a reflectometer, the following equation is given.
FSN = (Rf−Rs) / Rf × 10
In formula: Rf: Reflectance meter value of paper before sucking exhaust gas
Rs: Reflectometer value of paper that sucks exhaust gas and adheres smoke

  In the evaluation of the fuel oil composition, the exhaust gas level at which premixed compression ignition combustion can be determined to be achieved preferably with a small amount of exhaust gas, smoke emission: 0.3 or less, NOx emission: 30 ppm or less, The amount of hydrocarbon emissions was assumed to be 3000 ppm or less.

As is apparent from Table 3, the requirements stipulated in the present invention, that is, the initial boiling point is 20 ° C to 135 ° C, the 50% distillation point is 60 ° C to 250 ° C, and the end point is 200 ° C to 350 ° C. The kinematic viscosity at 30 ° C. is 0.4 mm ² / s or more and 3.0 mm ² / s or less, the sulfur content is 10 mass ppm or less, the cetane number of the whole fuel is 30 or more and 50 or less, and the boiling point is less than 150 ° C. the cetane number of distillate is 10 or more 45 or less and a boiling point Ri der cetane number of 0.99 ° C. or more fractions of at least 30 95 or less, and a fraction of the cetane number having a boiling point of less than 150 ℃ (150-CN ) And the cetane number (150 + CN) of the fraction having a boiling point of 150 ° C. or higher [(150−CN) / (150 + CN)] satisfying the requirement that the ratio is 1 or less , Preliminarily with low emissions Mixed compression self-ignition combustion can be achieved, and the combustion noise exhibits much better noise characteristics than the combustion noise of fuel oil compositions that do not meet the requirements of Comparative Examples 1-5.

Claims (2)

2. Initial boiling point is 20 ° C. or higher and 135 ° C. or lower, 50% distillation point is 60 ° C. or higher and 250 ° C. or lower, end point is 200 ° C. or higher and 350 ° C. or lower, and kinematic viscosity at 30 ° C. is 0.4 mm ² / s or higher. 0 mm ² / s or less, the sulfur content is 10 mass ppm or less, the cetane number of the whole fuel is 30 or more and 50 or less, and the cetane number of the fraction having a boiling point of less than 150 ° C. is 10 or more and 45 or less, boiling point Ri der cetane number of 0.99 ° C. or more fractions of at least 30 95 or less, and a fraction of the cetane number having a boiling point of less than 150 ℃ (150-CN) and a boiling point of 0.99 ° C. or more fractions of cetane number ( 150 + CN) ratio [(150-CN) / (150 + CN)] is 1 or less, The fuel oil composition for compression self-ignition engines characterized by the above-mentioned. The fuel oil composition for a compression self-ignition engine according to claim 1 , wherein the end point is 200 ° C or higher and 300 ° C or lower.