BACKGROUND OF THE INVENTION
[0001] The present invention relates to fuels for homogeneous charge compression ignition
engines, more specifically to those capable of controlling the combustion reaction
during homogeneous charge compression combustion to improve the engine thermal efficiency.
[0002] Nowadays, two types of engines have been widely used, one of which is a spark ignition
gasoline engine and the other of which is a compression ignition engine (diesel engine).
[0003] For the spark ignition gasoline engine, fuel is injected into the intake port or
the combustion chamber, and premixed gas of air fuel mixture is formed. Then the premixed
gas is ignited by a spark plug and combusted. The fuel is required to have high vaporization
and low auto-ignitability characteristics. Since the spark ignition gasoline engine
emits nitrogen oxides (NOx), hydrocarbons (HC) and carbon monoxide, a three-way catalyst
has been widely used for purifying these emissions. However, an exhaust gas purification
system such as a three-way catalyst is only applicable to a range where the air-fuel
ratio is in a very narrow range of stoichiometric air-fuel ratio and it is the causes
of low thermal efficiency and poor fuel consumption comparing with the compression
ignition diesel engine.
[0004] For the diesel engine, a diesel fuel is directly injected into the cylinder and mixed
with the air during compression stroke. The air-fuel mixture is auto-ignited by increasing
the temperature and pressure by piston compression. The diesel fuel is required to
have high ignitability characteristics. The compression auto-ignition diesel engine
is excellent in fuel consumption and thermal efficiency but has disadvantages of NOx
and soot emissions caused by the heterogeneous air fuel mixture. Furthermore, severe
control of an after treatment system such as an oxidation catalyst, NOx trap, a diesel
particulate filter or an SCR system is required to reduce NOx and soot to meet political
regulations.
[0005] Therefore, the conventional spark ignition gasoline engine can purify the exhaust
gas to a certain extent but has problems regarding fuel consumption and thermal efficiency.
On the contrary, the diesel engine is excellent in fuel consumption and has high thermal
efficiency, but it has problems of emission of NOx. Therefore, a homogeneous charge
compression ignition engine has been studied to achieve low NOx exhaust gas, excellent
fuel consumption and high thermal efficiency.
[0006] For the homogeneous charge compression ignition engine, the fuel is injected into
the intake port or combustion chamber at an injection pressure of 20 MPa or lower,
which is extremely lower than the diesel engine and the fuel injection is completed
at a crank angle of 60 degrees before the top dead center so that a premixed air-fuel
mixture is combusted by auto-ignition but not by spark ignition. The homogeneous charge
compression ignition engine takes a longer period to prepare a well-mixed air-fuel
mixture in the cylinder, comparing with the diesel engine. Therefore, for the homogeneous
charge compression ignition engine, a high temperature combustion region, the temperature
of which is higher than 2200K, is not locally formed in the cylinder and this is the
cause of low NOx emission characteristics (less than 10 ppm by mass) without a reduction
catalyst. The thermal efficiency and fuel consumption of the homogeneous charge compression
ignition engine are equivalent to those of the diesel engine.
[0007] Various fuels for the homogeneous charge compression auto-ignition combustion engine
have been proposed, focusing on various indices such as ignitability, volatility,
cetane number and octane number (for example, see Patent Documents 1 to 13 below).
However, more optimum and suitable fuels for homogeneous charge compression ignition
have been demanded from the point of engine performances.
Patent Document 1: Japanese Patent Laid-Open
Publication No. 2004-919657
Patent Document 2: Japanese Patent Laid-Open
Publication No. 2004-919658
Patent Document 3: Japanese Patent Laid-Open
Publication No. 2004-919659
Patent Document 4: Japanese Patent Laid-Open
Publication No. 2004-919660
Patent Document 5: Japanese Patent Laid-Open
Publication No. 2004-919661
Patent Document 6: Japanese Patent Laid-Open
Publication No. 2004-919662
Patent Document 7: Japanese Patent Laid-Open
Publication No. 2004-919663
Patent Document 8: Japanese Patent Laid-Open
Publication No. 2004-919664
Patent Document 9: Japanese Patent Laid-Open
Publication No. 2004-919665
Patent Document 10: Japanese Patent Laid-Open
Publication No. 2004-919666
Patent Document 11: Japanese Patent Laid-Open
Publication No. 2004-919667
Patent Document 12: Japanese Patent Laid-Open
Publication No. 2004-919668
Patent Document 13: Japanese Patent Laid-Open
Publication No. 2004-315604
BRIEF SUMMARY OF THE INVENTION
[0008] For the homogeneous charge compression ignition engine (hereinafter referred to as
"HCCI combustion"), a well mixed air-fuel mixture is compressed by a piston which
raises the temperature and pressure, and the auto-ignition is initiated. For the HCCI
engine, the engine operation is restricted at a low load range because of heavy engine
noises (high maximum pressure rise rate) over the middle range of the engine load.
[0009] The present invention has an object to provide a fuel for the HCCI engine that enhances
the HCCI operational range to a higher load range.
[0010] The present invention can be achieved by mixing high ignitability hydrocarbons (mainly
C5 to C10 normal paraffins) and C6-C11 aromatics whose benzene rings start to break
over 1100K or higher, where the hot flame reaction starts. The fuel of the present
invention can prolong the combustion period, reduce the maximum pressure rise rate
and enables the HCCI engine to operate in a higher load rage.
[0011] That is, the present invention relates to a fuel for an HCCI engine satisfying all
of the following characteristic requirements (1) to (6) and the following requirement
(7) or (8):
- (1) the total content of C5 to C10 normal paraffins is 25 percent by volume or more,
and 70 percent by volume or less;
- (2) the total content of C6 to C11 aromatic hydrocarbons is 30 percent by volume or
more, and 75 percent by volume or less;
- (3) the content of olefinic hydrocarbons is 20 percent by volume or less;
- (4) the content of oxygenates is 5 percent by mass or less in terms of oxygen;
- (5) the research octane number is 70 or greater, and less than 92;
- (6) the initial boiling point and end point in distillation characteristics are 30°C
or higher and 220°C or lower, respectively;
- (7) the averaged maximum pressure rise rate of the fuel over continuous 400 cycles
is smaller by 15 percent or more, comparing with that of a primary reference fuel
(PRF) which exhibits the same indicated mean effective pressure (IMEP) and crank angle
of 50% burn of high temperature heat release (HTHR CA50) as the fuel under the same
engine operating conditions such as compression ratio of the engine, engine speed,
boost pressure, temperature in the intake manifold, air flow rate, intake-exhaust
valve timing, EGR rate and fuel injection initiation timing; and
- (8) the average IMEP of the fuel over continuous 400 cycles is increased by 20 percent
or more, comparing with a primary reference fuel (PRF) with the same research octane
number as the fuel, the IMEPs of the fuel and PRF being measured at the same maximum
pressure rise rate under the same engine operating conditions such as compression
ratio of the engine, engine speed, boost pressure, temperature in the intake manifold,
air flow rate, intake-exhaust valve timing, EGR rate and fuel injection initiation
timing.
[0012] [Effects of the Invention]
[0013] The fuel of the present invention can lower the maximum pressure rise rate of homogeneous
charge compression ignition combustion and thus achieves a quiet engine combustion.
Furthermore, the fuel can enhance the engine output by 20 percent or more under the
same maximum pressure rise rate, comparing with the conventional fuels.
BRIEF DESCRIPTION OF THE SEVERAL VIEWS OF THE DRWAINGS
[0014] The foregoing summary, as well as the following detailed description of the invention
will be better understood when read in conjunction with the appended drawings. Figures
1-11 are the comparisons of the tangible engine test data obtained by fuels according
to the present invention and the comparative test results obtained by other fuels.
For the purpose of illustrating the invention, there are shown in the drawings embodiments
which are presently preferred. It should be understood, however, that the invention
is not limited to the precise arrangements and instrumentalities shown.
[0016] Fig. 1 shows how the HCCI combustion (dual phase high temperature heat release combustion)
of the present invention occurs.
[0017] Fig. 2 indicates the relation between averaged HTHR CA50s and IMEPs over 400 cycles
under the operation conditions in Example 1.
[0018] Fig. 3 shows the change in maximum pressure rise rate at Point 1 over 400 cycles.
[0019] Fig. 4 shows the change in maximum pressure rise rate at Point 2 over 400 cycles.
[0020] Fig. 5 shows the change in maximum pressure rise rate at Point 3 over 400 cycles.
[0021] Fig. 6 shows the in-cylinder pressure at measurement Point A in Figure 2.
[0022] Fig. 7 shows the heat release rate at measurement Point A in Figure 2.
[0023] Fig. 8 shows the in-cylinder pressure at measurement Point B in Figure 2.
[0024] Fig. 9 shows the heat release rate at measurement Point B in Figure 2.
[0025] Fig. 10 shows the in-cylinder pressure at measurement Point C in Figure 2.
[0026] Fig. 11 shows the heat release rate at measurement Point C in Figure 2.
DETAILED DESCRIPTION OF THE INVENTION
[0027] The present invention will be described in more detail below.
[0028] The fuel of the present invention is suitable for a homogeneous charge compression
ignition engine (hereinafter the homogeneous charge compression ignition is abbreviated
as HCCI). The term "HCCI" herein denotes a combustion mode wherein fuel is combusted
by auto-ignition under the following conditions (A), (B) and (C):
- (A) fuel injection pressure: 20 MPa or lower;
- (B) fuel injection position: the intake port and/or the direct injection into the
cylinder; and
- (C) timing of completion of fuel injection: 60 degrees crank angle before the top
dead center.
[0029] The HCCI is lower in (A) fuel injection pressure than conventional diesel engines
and longer in (C) time period after the end of injection to the initiation of combustion
to prepare a well-mixed air fuel mixture in the cylinder, than conventional diesel
engines. Therefore, for the HCCI engine, a high temperature combustion region, the
temperature of which is higher than 2200k, is not locally formed in the cylinder and
this is the cause of low NOx emission characteristics (less than 10 ppm by mass) without
a reduction catalyst.
[0030] The homogeneous charge compression auto-ignition combustion mode may also be referred
to as HCCI (Homogeneous Charge Compression Ignition), PCCI (Premixed Charge Compression
Ignition), PCI (Premixed Compression Ignition), CAI (Controlled Auto-Ignition) or
AR (Active Radical (Combustion)).
[0031] The fuel of the present invention is suitably used in an HCCI engine. However, the
fuel is also applicable to the following types of engines such as HCCI-SI gasoline
engines (SI: spark ignition), HCCI-CI diesel engines (CI: compression ignition), and
electric motored hybrid engines with HCCI, HCCI-SI and HCCI-DI engines.
[0032] When fuel auto-ignites, low temperature heat release (LTHR) reaction occurs first
and then high temperature heat release (HTHR) reaction occurs. The fuel for an HCCI
engine of the present invention is characterized by the combination of a fuel (normal
paraffin rich fuel) that has a high decomposability and a fuel (aromatic and olefin
rich fuel) that has a low decomposability. Therefore, the fuel of the present invention
exhibits a dual phase high temperature heat release combustion as shown in Fig. 1.
The paraffinic hydrocarbons are first decomposed and oxidized during cool frame and
blue flame periods and then decomposition and oxidation of the aromatic radicals and
aromatic hydrocarbons starts during a hot flame period.
[0033] The fuel of the present invention needs to satisfy the following characteristics
requirements (1) to (6):
- (1) the total content of C5 to C10 normal paraffins is 25 percent by volume or more
and 70 percent by volume or less, preferably 30 percent by volume or more and 50 percent
by volume or less because normal paraffinic hydrocarbons of C4 or less can not exhibit
sufficient low temperature heat release (LTHR) reaction while hydrocarbons of C11
or more has a high boiling point and are not suitable for an HCCI engine;
- (2) the total content of C6 to C11 aromatic hydrocarbons is 30 percent by volume or
more and 75 percent by volume or less, preferably 50 percent by volume or more and
65 percent by volume or less because hydrocarbons of C12 or more are poor in volatility
and not suitable for an HCCI engine and the presence of more than 75 percent by volume
of aromatics restricts the operational range against engine speed and load;
- (3) the content of an olefin is 20 percent by volume or less, preferably 10 percent
by volume or less;
- (4) the content of oxygenates is 5 percent by mass or less in terms of oxygen;
- (5) the research octane number is 70 or greater and less than 92, preferably 70 or
greater and 86 or less; and
- (6) the initial boiling point in distillation is 30°C or higher, and end point in
distillation is 220°C or lower, preferably 150°C or lower.
[0034] The definition of the hydrocarbon contents used herein denotes the value measured
in accordance with JIS K 2536 "Liquid petroleum products-Testing method of components"
using gas chromatography. The term "normal paraffin" used herein denotes straight-chain
hydrocarbon containing no naphthene (cyclic saturated hydrocarbon).
[0035] In addition to the foregoing requirements, the fuel of the present invention needs
to satisfy the following requirement (7) or (8):
[0036] (7) the averaged maximum pressure rise rate of the fuel over continuous 400 cycle
is smaller by 15 percent or more, preferably 20 percent or more, comparing with that
of a primary reference fuel (PRF) which exhibits the same indicated mean effective
pressure (IMEP) and crank angle of 50% burn of high temperature heat release combustion
(HTHR CA50) as the fuel under the same engine operating conditions (compression ratio
of the engine, engine speed, boost pressure, temperature in the intake manifold, air
flow rate, intake-exhaust valve timing, EGR rate and fuel injection initiation timing).
[0037] The terms "the same mean effective pressure and crank angle of 50% burn of high temperature
heat release combustion" are defined as being within ±20 kPa in indicated mean effective
pressure and within ±0.8 degree crank angle in HTHR CA 50, respectively, comparing
with a comparative fuel, i.e., PRF. The "PRF" is an abbreviation of primary reference
fuel used for the measurement of octane numbers. For example, "PRF80" means a fuel
with a research octane number of 80, produced by mixing 80 percent by volume of iso-octane
and 20 percent by volume of normal heptane. The method of measuring the mean effective
pressure and definition of HTHR CA50 are described in an SAE technical paper, No.
SAE2006-01-0207.
[0038] (8) the averaged IMEP of the fuel over continuous 400 cycles is increased by 20 percent
or more, preferably 25 percent or more, more preferably 50 percent, comparing with
that of a primary reference fuel (PRF) with the same research octane number as the
fuel, the IMEPs of the fuel and PRF being measured at the same maximum pressure rise
rate under the same engine operating conditions (compression ratio of the engine,
engine speed, boost pressure, temperature in the intake manifold, air flow rate, intake-exhaust
valve timing, EGR rate and fuel injection initiation timing).
[0039] The measurement inaccuracy in the maximum pressure rise rate is defined as being
within ±4 kPa/deg comparing with PRF.
[0040] There is no particular restriction on the sulfur content of the fuel. However, the
sulfur content is preferably 10 ppm by mass or less, and with the objective of keeping
the performances of a catalyst in a high level, more preferably 5 ppm by mass, most
preferably 1 ppm by mass or less. A sulfur content of more than 10 ppm by mass is
not preferable because an exhaust gas-purifying catalyst equipped in an engine is
poisoned with sulfur, resulting in a poor exhaust gas-purifying performance. The sulfur
content used herein denotes the value measured in accordance with JIS K 2541 "Crude
oil and petroleum products-Determination of sulfur content".
[0041] The fuel of the present invention contains hydrocarbons as the main component but
may further contain oxygenates such as ethers, alcohols, ketones, esters, and glycols.
Examples of the oxygenates include methanol, ethanol, normalpropyl alcohol, isopropyl
alcohol, normalbutyl alcohol, isobutyl alcohol, dimethyl ether, diisopropyl ether,
methyl-tert-butyl ether (MTBE), ethyl-tert-butyl ether (ETBE), tert-amyl methyl ether
(TAME), tert-amyl ethyl ether, fatty acid methyl ester, and fatty acid ethyl ester.
[0042] The fuel of the present invention can reduce unburnt hydrocarbon (HC) and fine particulate
matters due to the presence of the foregoing oxygenates. When the fuel contains a
biomass-originating oxygenate, it contributes to reduce carbon dioxide. However, as
the case may be, the oxygenates cause an increase in nitrogen compounds. Therefore,
the content of the oxygenates is preferably 5 percent by mass or less in terms of
oxygen on the basis of the total mass of the fuel.
[0043] There is no particular restriction on the base oil of the fuel of the present invention
as long as the fuel characteristics described above can be attained. For example,
the base oil may be any one or more of base oils selected from naphtha fractions produced
by atmospheric distillation of crude oil (full-range naphtha); light fractions of
naphtha (light naphtha); heavy fractions of naphtha (heavy naphtha); desulfurized
full-range naphtha produced by desulfurization of full-range naphtha; desulfurized
light naphtha produced by desulfurization of light naphtha; desulfurized heavy naphtha
produced by desulfurization of heavy naphtha; isomerized gasolines produced by converting
light naphthas to isoparaffin in an isomerization unit; alkylates produced by addition
(alkylation) of lower olefins to hydrocarbons such as iso-butane; reformed gasolines
produced by a catalytic reforming process; raffinates which are residues produced
by extracting aromatic components from reformed gasolines; light reformed gasolines
that are light fractions of reformed gasolines; middle reformed gasolines that are
middle fractions of reformed gasolines; heavy reformed gasolines that are heavy fractions
of reformed gasolines; cracked gasolines produced by catalytic cracking or hydrocracking;
light fraction of cracked gasolines; heavy fraction of cracked gasolines; straight
gas oils and straight kerosene produced through an atmospheric distillation unit for
crude oil; vacuum gas oils produced by processing straight heavy oil or residue produced
through an atmospheric distillation unit, in a vacuum distillation unit; catalytically
cracked or hydrocracked gas oils and kerosenes produced by catalytically cracking
or hydrocracking vacuum heavy gas oils or desulfurized heavy oils; hydrorefined gas
oils, hydrodesulfurized gas oils or hydrorefined kerosenes produced by hydrorefining
the foregoing petroleum hydrocarbons; and naphtha fractions, kerosene fractions and
gas oil fractions of GTL (Gas to liquids) produced by F-T (Fischer-Tropsch) synthesizing
natural gas that have been decomposed to carbon monoxide or hydrogen.
[0044] The fuel of the present invention may contain known fuel additives if necessary.
Examples of such fuel additives include friction modifiers such as amide compounds
of carboxylic acids and alcohol amines; detergent-dispersants such as succinimide,
polyalkyl amine, and polyether amine; anti-oxidants such as N,N'-diisopropyl-p-phenylene
diamine, N,N'-diisobutyl-p-phenylene diamine, 2,6-di-t-butyl-4-methyl phenol and hindered
phenols; metal deactivators such as amine carbonyl condensation compounds, for example,
N,N'-disalicylidene-1,2-diamino propane; surface ignition inhibitors such as organic
phosphorus compounds; anti-icing agents such as polyhydric alcohols and ethers thereof;
combustion improvers such as alkali or alkaline metal salts of organic acids and sulfuric
esters of higher alcohols; anti-static additives such as anionic, cationic, and amphoteric
surface active agents; coloring agents such as azo dye; rust inhibitors such as organic
carboxylic acids, their derivatives and alkenyl succinic acid esters; water draining
agents such as sorbitan esters; cetane number improvers such as nitrate esters and
organic peroxides; lubricity improvers such as carboxylic acid-, ester-, alcohol-
and phenol-based lubricity improvers; silicone-based defoaming agents; cold flow improvers
such as ethylene vinyl acetate copolymers and alkenylsuccinic imides; markers such
as quinizarin and coumarin; and odorants. These additives may be added alone or in
combination and are desirously added so that the total amount of these additives is
0.5 percent by mass or less, more preferably 0.2 percent by mass on the basis of the
total amount of the fuel. The total amount of the additives denotes the amount in
terms of their effective components.
[0046] Hereinafter, the present invention will be described in more detail by way of the
following examples and comparative examples, which should not be construed as limiting
the scope of the invention.
[0047] Fuels of the present invention (Examples 1 and 2) and those for comparison (Comparative
Examples 1 and 2) were produced in accordance with the formulations set forth in Table
1 below in a conventional manner. Table 1 also shows the ratio of hydrocarbons and
characteristics of each of the resulting fuel.
[0048]
Table 1
| Items |
Fuels used in Comparative Examples |
Fuels used in Examples |
| |
|
PRF75 |
PRF80 |
PRF85 |
PRF90 |
NDB75 |
NDB80 |
NDB85 |
NDB90 |
NMP75 |
NMP80 |
NMP85 |
NCP75 |
NCP80 |
NTL70 |
NTL75 |
NTL80 |
NTL85 |
| Density 15C |
g/cm3 |
0.6936 |
0.694 |
0.6942 |
0.6945 |
0.7043 |
0.7057 |
0.7071 |
0.7085 |
0.6746 |
0.6735 |
0.6725 |
0.721 |
0.724 |
0.792 |
0.799 |
0.807 |
0.815 |
| RON |
|
75.0 |
80.0 |
85.0 |
90.0 |
75.0 |
80.0 |
85.0 |
89.3 |
75.3 |
80.0 |
85.0 |
74.5 |
79.8 |
70.0 |
74.5 |
80.0 |
84.8 |
| C% |
wt% |
84.06 |
84.07 |
84.08 |
84.09 |
84.77 |
84.84 |
84.92 |
84.99 |
85.09 |
85.19 |
85.28 |
84.88 |
84.95 |
88.38 |
88.69 |
89.00 |
89.31 |
| H% |
wn% |
15.94 |
15.93 |
15.92 |
15.91 |
15.23 |
15.16 |
15.08 |
15.01 |
14.91 |
14.81 |
14.72 |
15.12 |
15.05 |
11.62 |
11.31 |
11.00 |
10.69 |
| H/C |
|
2.275 |
2.273 |
2.271 |
2.270 |
2.156 |
2.144 |
2.132 |
2.119 |
2.102 |
2.087 |
2.071 |
2.138 |
2.126 |
1.578 |
1.530 |
1.483 |
1.437 |
| Stoic A/F |
|
15.13 |
15.13 |
15.12 |
15.12 |
14.97 |
14.95 |
14.93 |
14.92 |
14.89 |
14.87 |
14.85 |
14.94 |
14.93 |
14.14 |
14.07 |
14.00 |
13.93 |
| Heating value |
kJ/kg |
44399 |
44388 |
44378 |
44367 |
44312 |
44291 |
44270 |
44249 |
44290 |
44270 |
44249 |
44122 |
44090 |
42101 |
41928 |
41759 |
41592 |
| n-Heptane |
vol% |
25.00 |
20.00 |
15.00 |
10.00 |
50.89 |
46.62 |
42.35 |
38.08 |
30.27 |
24.98 |
19.69 |
45.57 |
41.39 |
44.82 |
40.31 |
35.80 |
31.29 |
| iso-Octane |
vol% |
75.00 |
80.00 |
85.00 |
90.00 |
|
|
|
|
|
|
|
|
|
|
|
|
|
| Diisobutylene |
vol% |
|
|
|
|
49.11 |
53.38 |
57.65 |
61.92 |
|
|
|
|
|
|
|
|
|
| 4Methyl-1-pentene |
vol% |
|
|
|
|
|
|
|
|
69.73 |
75.02 |
80.31 |
|
|
|
|
|
|
| Toluene |
vol% |
|
|
|
|
|
|
|
|
|
|
|
|
|
55.18 |
59.69 |
64.20 |
68.71 |
| Cyclopentane |
vol% |
|
|
|
|
|
|
|
|
|
|
|
54.43 |
58.61 |
|
|
|
|
| n-Heptane |
mass% |
24.78 |
19.81 |
14.85 |
9.90 |
49.77 |
45.52 |
41.26 |
37.02 |
30.88 |
25.51 |
20.13 |
43.46 |
39.33 |
39.05 |
34.76 |
30.55 |
26.43 |
| iso-Octane |
mass% |
75.22 |
80.19 |
85.15 |
90.10 |
|
|
|
|
|
|
|
|
|
|
|
|
|
| Diisobutylene |
mass% |
|
|
|
|
50.23 |
54.48 |
58.74 |
62.98 |
|
|
|
|
|
|
|
|
|
| 4Methyl-1-pentene |
mass% |
|
|
|
|
|
|
|
|
69.12 |
74.49 |
79.87 |
|
|
|
|
|
|
| Toluene |
mass% |
|
|
|
|
|
|
|
|
|
|
|
|
|
60.95 |
65.24 |
69.45 |
73.57 |
| Cyclopentane |
mass% |
|
|
|
|
|
|
|
|
|
|
|
56.54 |
60.67 |
|
|
|
|
[0049] (Engine Specifications)
[0050] Type of Engine: in-line 4 cylinder HCCI engine with a compression ratio of 15. The
engine specifications are described in the document "SAE2006-01-0207" (published in
April, 2006)
[0052] (Engine operation conditions)
[0053] The engine was operated at an engine speed of 1000 rpm, an absolute boost pressure
of 155 kPa and an intake manifold temperature of 58°C. The experiment described below
was carried out for each fuel under the same engine conditions such as compression
ratio, engine speed, boost pressure, intake manifold temperature, air flow rate, intake-exhaust
valve timing and EGR rate except that the fuel injection quantity was varied.
[0055] Fig. 2 shows the chart of 400 cycle averaged crank angle of 50% burn of high temperature
heat release (HTHR CA50) and indicated mean effective pressure (IMEP) obtained by
driving the engine using various fuels. Where fuels with the substantially same IMEP
and HTHR gathered were selected as Points 1, 2 and 3, and the change in maximum pressure
rise rate over 400 cycles in each of the points were measured (the detail of this
experiment should be referred to "SAE2008-01-0007" published in April, 2008).
[0056] Fig. 3 shows the changes in maximum pressure rise rate over 400 cycles at Point 1,
Fig. 4 shows the changes in maximum pressure rise rate over 400 cycles at Point 2,
and Fig. 5 shows the changes in maximum pressure rise rate over 400 cycles at Point
3. The details are set forth in Tables 2, 3 and 4.
[0057] It is confirmed that NTL series fuels (NTL70, NTL75) corresponding to the fuel of
the present invention are reduced in maximum pressure rise rate by 20 percent or greater,
comparing with PRF series fuels (PRF90, PRF85) when they were used under the same
operation conditions (same IMEP, same HTHR CA50). Further, when the fuels other than
Comparative Example 1 (NDB fuel, NMP fuel) are compared with the NTL series fuels
of Example 1, none of the other fuels can reduce the maximum pressure rise rate as
much as the fuels of Example 1. In the present invention, the rapid combustion of
the fuel is avoided by utilizing the difference in temperatures at which a component
containing mainly a paraffinic fuel and a component containing mainly an aromatic
fuel ignite, thereby achieving HCCI operation wherein the maximum pressure rise rate
is suppressed.
[0058]
Table 2
| |
Fuel |
Maximum Pressure Rise rate kPa/deg |
Indicated Mean Effective Pressure kPa |
HTHR CA50 CA deg ATDC |
| Comparative Example 1-1 |
PRF90 |
799.7 |
504.5 |
1.34 |
| Comparative Example 1-2 |
NDB90 |
902.7 |
498 |
1.3 |
| Comparative Example 1-3 |
NMP85 |
903.1 |
501.6 |
1.6 |
| Example 1-1 |
NTL75 |
599.9 |
500.4 |
1.63 |
| Reduction rate in maximum pressure rise rate of NTL75 (against PRF90) : 24.9% |
[0059]
Table 3
| |
Fuel |
Maximum Pressure Rise rate kPa/deg |
Indicated Mean Effective Pressure kPa |
HTHR CA50 CA deg ATDC |
| Comparative Example 1-4 |
PRF85 |
399.6 |
299.9 |
2.05 |
| Comparative Example 1-5 |
NDB85 |
399.8 |
280.7 |
2.38 |
| Comparative Example 1-6 |
NMP80 |
399.4 |
284.7 |
2.3 |
| Example 1-2 |
NTL70 |
302.6 |
313 |
2.74 |
| Reduction rate in maximum pressure rise rate of NTL70 (against PRF85) : 24.3% |
[0060]
Table 4
| |
Fuel |
Maximum Pressure Rise rate kPa/deg |
Indicated Mean Effective Pressure kPa |
HTHR CA50 CA deg ATDC |
| Comparative Example 1-7 |
PRF85 |
900.8 |
485.9 |
-1.15 |
| Example 1-3 |
NTL70 |
699.8 |
494.9 |
-0.91 |
| Reduction rate in maximum pressure rise rate of NTL70 (against PRF85) : 22.3% |
[0063] The following fuels with the same research octane number were prepared (when the
difference in the research octane number between PRF series fuels and NTL series fuels
measured on a CFR (Cooperative Fuel Research) engine in accordance with JIS K 2280
is within 3, it was regarded as inaccuracy).
[0064] (1) Fuels with a research octane number of 75
[0065] (Comparative Examples) PRF75, NDB75, NMP75, NCP75
[0067] (2) Fuels with a research octane number of 80
[0068] (Comparative Examples) PRF80, NDB80, NMP80, NCP80
[0070] (3) Fuels with a research octane number of 85
[0071] (Comparative Examples) PRF85, NDB85, NMP85,
[0073] (Engine operation conditions)
[0074] The engine was operated at an engine speed of 1000 rpm, an absolute boost pressure
of 155 kPa and an intake manifold temperature of 58°C. An experiment was carried out
for each fuel under the same engine conditions such as compression ratio, engine speed,
boost pressure intake pipe temperature, air flow rate, intake-exhaust valve timing
and EGR rate to obtain experimental data of each fuel, at the same averaged maximum
pressure rise rate over 400 cycles.
[0075] For fuels with a research octane number of 75, the experimental data were obtained
by measurement at a maximum pressure rise rate of 800 kPa/deg (measurement condition
A).
[0076] For fuels with a research octane number of 80, the experimental data were obtained
by measurement at a maximum pressure rise rate of 600 kPa/deg (measurement condition
B).
[0077] For fuels with a research octane number of 85, the experimental data were obtained
by measurement at a maximum pressure rise rate of 400 kPa/deg (measurement condition
C).
[0079] The average in-cylinder pressure and heat release rate over 400 cycles of each fuel
measured under the conditions A, B and C are shown in Figs. 6 to 11 and set forth
in Tables 5 to 7.
[0080]
Table 5
| |
Fuel |
Maximum Pressure Rise rate kPa/deg |
Indicated Mean Effective Pressure kPa |
| Comparative Example 2-1 |
PRF75 |
800.7 |
417.2 |
| Comparative Example 2-2 |
NDB75 |
800.4 |
402.5 |
| Comparative Example 2-3 |
NMP75 |
800.1 |
410.6 |
| Example 2-1 |
NTL75 |
800.0 |
535.0 |
| Comparative Example 2-4 |
NCP75 |
801.5 |
379.6 |
| Reduction rate in indicated mean effective pressure of NTL75 (against PRF75) : 28.2% |
[0081]
Table 6
| |
Fuel |
Maximum Pressure Rise rate kPa/deg |
Indicated Mean Effective Pressure kPa |
| Comparative Example 2-5 |
PRF80 |
600.6 |
356.7 |
| Comparative Example 2-6 |
NDB80 |
599.3 |
335.0 |
| Comparative Example 2-7 |
NMP80 |
600.3 |
361.3 |
| Example 2-2 |
NTL80 |
601.1 |
576.6 |
| Comparative Example 2-8 |
NCP80 |
599.7 |
372.6 |
| Reduction rate in indicated mean effective pressure of NTL80 (against PRF80) : 61.6% |
[0082]
Table 7
| |
Fuel |
Maximum Pressure Rise rate kPa/deg |
Indicated Mean Effective Pressure kPa |
| Comparative Example 2-9 |
PRF85 |
399.8 |
299.9 |
| Comparative Example 2-10 |
NDB85 |
399.6 |
280.7 |
| Comparative Example 2-11 |
NMP85 |
401.1 |
339.4 |
| Example 2-3 |
NTL85 |
401.0 |
640.4 |
| Reduction rate in indicated mean effective pressure of NTL85 (against PRF85) : 113.5% |
[0083] All of Figs. 6 to 11 show that NTL series fuels (NTL75, NTL80, NTL85) according to
the present invention exhibited an increase by 28 to 113 percent in indicated mean
effective pressure, compared with comparative fuels (PRF series fuels, NDB series
fuels, NMP series fuels, NCP series fuels) under the same maximum pressure rise rate
condition. As shown in Figs. 7, 9 and 11, this is because the fuel of the present
invention prolongs combustion period by utilizing difference in ignition temperature
between a component containing mainly a paraffinic fuel and a component containing
mainly an aromatic fuel so as to avoid the rapid combustion of the fuel and thus the
more fuel can be combusted under the same maximum pressure rise rate, thereby increasing
the heat release rate.
1. A fuel for a homogeneous charge compression auto-ignition combustion engine satisfying
all of the following characteristic requirements (1) to (6) and the following requirement
(7) or (8):
(1) the total content of C5 to C10 normal paraffins is 25 percent by volume or more,
and 70 percent by volume or less;
(2) the total content of C6 to C11 aromatic hydrocarbons is 30 percent by volume or
more, and 75 percent by volume or less;
(3) the content of olefinic hydrocarbons is 20 percent by volume or less;
(4) the content of oxygenates is 5 percent by mass or less in terms of oxygen;
(5) the research octane number is 70 or greater, and less than 92;
(6) the initial boiling point and end point in distillation characteristics are 30°C
or higher and 220°C or lower, respectively;
(7) the averaged maximum pressure rise rate of the fuel over continuous 400 cycles
is smaller by 15 percent or more, comparing with that of a primary reference fuel
(PRF) which exhibits the same indicated mean effective pressure (IMEP) and crank angle
of 50% burn of high temperature heat release combustion (HTHR CA50) as the fuel under
the same engine operating conditions such as compression ratio of the engine, engine
speed, boost pressure, temperature in the intake manifold, air flow rate, intake-exhaust
valve timing, EGR rate and fuel injection initiation timing; and
(8) the averaged IMEP of the fuel over continuous 400 cycles is increased by 20 percent
or more, comparing with that of a primary reference fuel (PRF) with the same research
octane number as the fuel, the IMEPs of the fuel and PRF being measured at the same
maximum pressure rise rate under the same engine operating conditions such as compression
ratio of the engine, engine speed, boost pressure, temperature in the intake manifold,
air flow rate, intake-exhaust valve timing, EGR rate and fuel injection initiation
timing.
2. The fuel for a homogeneous charge compression auto-ignition combustion engine according
to claim 1, wherein the sulfur content of the fuel is 10 ppm by mass or less.
3. The fuel for a homogeneous charge compression auto-ignition combustion engine according
to claim 1, comprising oxygenates selected from the group consisting of methanol,
ethanol, normalpropyl alcohol, isopropyl alcohol, normalbutyl alcohol, isobutyl alcohol,
dimethyl ether, diisopropyl ether, methyl-tert-butyl ether (MTBE), ethyl-tert-butyl
ether (ETBE), tert-amyl methyl ether (TAME), tert-amyl ethyl ether, fatty acid methyl
ester, and fatty acid ethyl ester.
4. The fuel for a homogeneous charge compression auto-ignition combustion engine according
to claim 1, wherein the fuel is also applicable to the following types of engines
selected from the group consisting of HCCI-SI gasoline engines (SI: spark ignition),
HCCI-CI diesel engines (CI: compression ignition), and electric motored hybrid engines
with HCCI, HCCI-SI and HCCI-DI engines.