BACKGROUND OF THE INVENTION
FIELD OF THE INVENTION
[0001] The present invention relates to a diesel fuel composition which can yield reduced
emissions of particulates (particulate matter) from a diesel engine.
RELATED ART
[0002] Particulates are one of the substances emitted from diesel engines which are subject
to emission restrictions. Particulates consist principally of carbon particles (soot)
and hydrocarbons and partially oxidized products resulting from incomplete combustion.
A certain reduction in particulate emissions can be achieved by optimization of the
combustion system of the diesel engine, but improvements in the diesel fuel are also
required.
[0003] To reduce the particulate emissions by adapting the diesel fuel composition, it is
known to be effective to reduce the content of distillate with a high boiling point,
sulfur content, or density to increase cetane number, and to reduce the content of
aromatic hydrocarbons, and in particular of polycyclic aromatic hydrocarbons. According
to the researches of the inventors of the present application, however, it has become
clear that the above countermeasures are not sufficient for particulate reduction.
SUMMARY OF THE INVENTION
[0004] An object of the present invention is to provide a diesel fuel composition with a
reduced content of aromatic compounds which can realize further reduction of particulate
emissions.
[0005] According to the researches of the present inventors, it has become clear that even
a diesel fuel composition which has a reduced content of aromatic compounds and a
lowered boiling point, does not necessarily yield a satisfactory reduction in particulate
emissions. Furthermore, the present inventors have discovered that in addition to
these two factors, the presence or absence of branch structures and the number of
branches in hydrocarbons have a large effect on the generation of particulate matter,
and have thus completed the invention.
[0006] In the diesel fuel composition for reduced particulate emission of the present invention,
the ratio of the total area of a group of peaks with a chemical shift in the range
of 33 ppm to 50 ppm with respect to the total area of a group of peaks with a chemical
shift in the range of 0 ppm to 50 ppm is equal to or less than 30 % in a
13C nuclear magnetic resonance spectrum (hereinafter referred to as "
13C-NMR spectrum").
[0007] In the
13C-NMR spectrum, as described in more detail below, peaks with chemical shifts in the
range of 0 to 50 ppm are due principally to carbon atoms constituting hydrocarbon
portions not including unsaturated bonds, and peaks with chemical shifts in the range
of 33 to 50 ppm are due principally to tertiary and quaternary carbon atoms within
saturated hydrocarbon portions having branches, or carbon atoms adjacent to such atoms.
And thus the total area of a group of peaks with a chemical shift in the range of
33 to 50 ppm corresponds to the presence or absence of branches, and the number of
branches.
[0008] When the ratio of the total area of a group of peaks with a chemical shift in the
range of 33 to 50 ppm with respect to the total area of the soup of peaks with a chemical
shift in the range of 0 to 50 ppm is equal to or less than a specified value, which
is specifically equal to or less than 30%, and more preferably equal to or less than
20%, the hydrocarbons in the diesel fuel composition having a branching structure
can be reduced. As a result, the amount of particulate matter in the exhaust gas can
be positively reduced.
[0009] In the diesel fuel composition of the present invention, the content of aromatic
compounds is preferably equal to or less than 25% by volume, and even more preferably
equal to or less than 20% by volume. By means of such a reduction in the content of
aromatic compounds, the amount of particulate matter can be further positively reduced.
Here, "aromatic compounds" include aromatic hydrocarbons and additives which include
aromatic rings and so forth. And the aromatic compounds comprise polycyclic aromatic
compounds and the content thereof is preferably equal to or less than 5 % by volume.
BRIEF DESCRIPTION OF THE DRAWINGS
[0010] Figs. 1A and 1B show
13C-NMR spectra for a first embodiment and a first comparative example.
[0011] Figs. 2A to 2E illustrate molecular structures and chemical shifts corresponding
to the peaks in the spectra shown in Figs. 1A and 1B.
[0012] Fig. 3 illustrates particulate measurements for the first embodiment and first comparative
example.
[0013] Fig. 4 illustrates other particulate measurements for the first embodiment and first
comparative example.
[0014] Fig. 5 shows the products of thermal decomposition and their concentrations obtained
using a flow reactor, for the first embodiment and first comparative example.
[0015] Fig. 6 shows the products of thermal decomposition and their concentrations obtained
using a flow reactor, for different isomers of hexane.
[0016] Fig. 7 is a graph showing the relationship between the initial reaction temperature
and soot conversion ratio in Experiment 1 carried out with a shock tube.
[0017] Fig. 8 is a graph showing the relationship between the initial reaction temperature
and soot conversion ratio in Experiment 2 carried out with a shock tube.
[0018] Fig. 9 is a graph showing the relationship between the initial reaction temperature
and soot conversion ratio in Experiment 3 carried out with a shock tube.
[0019] Fig. 10 is a graph showing the relationship between the initial reaction temperature
and soot conversion ratio in Experiment 4 carried out with a shock tube.
[0020] Fig. 11 is a graph showing the relationship between the initial reaction temperature
and soot conversion ratio in Experiment 5 carried out with a shock tube.
[0021] Fig. 12 is a graph comparing the soot conversion ratios at the peaks respectively
shown in Figs. 7 to 11.
DESCRIPTION OF PREFERRED EMBODIMENTS
[0022] The present invention is now described in terms of a preferred embodiment, with reference
to specific data.
[0023] Figs. 1A and 1B show
13C-NMR spectra, Fig. 1A being the spectrum for a diesel fuel composition embodying
the present invention (first embodiment), and Fig. 1B the spectrum for a comparative
diesel fuel composition (first comparative example).
[0024] In the
13C-NMR spectrum of the present invention, the percentage ratio

of the total area
S2 of the group of peaks
e with a chemical shift in the range of 33 to 50 ppm with respect to the total area
S1 of the group of peaks
P1 with a chemical shift in the range of 0 to 50 ppm is equal to or less than 30%, and
preferably equal to or less than 20%. It should be noted that in Figs. 1A and 1B the
group of peaks
P2 in the spectrum corresponds to the peaks for the solvent.
[0025] In the spectra of Figs. 1A and 1B, of the peaks belonging to group
P1, the prominent peaks
a to
d correspond, as shown in Fig. 2A, to particular carbon atoms in unbranching saturated
hydrocarbon portions. It should be noted that in Figs. 2A to 2E the numerals associated
with particular carbon atoms indicate the corresponding chemical shifts. The peaks
belonging to the group
e with chemical shifts in the range of 33 to 50 ppm, as shown in part in Figs. 2B to
2E, correspond to tertiary and quaternary carbon atoms within branching molecules,
or carbon atoms adjacent to such atoms. Molecular structures belonging to the group
of peaks
e are not limited to those shown in Figs. 2B to 2E, and many other examples exist.
Moreover, this is well known, and is disclosed in the literature (for example,
13C-NMR Data Book, edited by Fumio Toda and Tokio Oshima).
[0026] Specifically, in the hydrocarbons constituting diesel fuel, saturated hydrocarbon
portions having tertiary or quaternary carbon atoms, for example hydrocarbons including
alkyl groups (C
nH
2n+1), alkenyl groups (C
nH
2n-1), alkynyl groups and alkadienyl groups (C
nH
2n-3), and alkatrienyl groups (C
nH
2n-5), or the like, produce peaks with a chemical shift in the range of 33 to 50 ppm as
above.
[0027] Table 1 shows the ratio of the area of each of the peaks
a to
d to the total peak area
S1, and the ratio of the total peak area
S2 of the group of peaks
e to the total peak area
S1 for the spectra of Figs. 1A and 1B. As is shown in Table 1, the proportion of the
total peak area for the group of peaks
e in the first embodiment of the present invention is 17.7%, whereas the proportion
of the total peak area for the group of peaks
e in the first comparative example is 30.5%.
Table 1
Sample |
Peak Area Proportion (%) |
|
Chemical Shift (ppm) |
a 14 |
b 22 |
c 29 |
d 32 |
e 33-50 |
First Embodiment |
|
9.0 |
11.2 |
31.6 |
8.3 |
17.7 |
First Comparative Example |
|
6.7 |
9.7 |
17.0 |
6.0 |
30.5 |
[0028] Sample diesel fuel compositions used in experiments, and the results of analysis
are now described.
Properties of the samples
[0029] Table 2 shows the properties of the diesel fuel composition of the first embodiment
of the present invention and the first comparative example. The first comparative
example is a commercial product (Sweden Class 1 diesel fuel (Shell Oil)), which with
the object of reducing particulate emission has a low content of aromatic compounds
and a reduced boiling point, compared with generally available commercial products.
[0030] The diesel fuel composition of the first embodiment with the object of reducing particulate
emission also has a low content of aromatic compounds and a reduced boiling point,
compared with generally available commercial products, but the content of aromatic
compounds is about 10% higher by volume, and in the T50 to T90 range, the diesel fuel
composition has boiling points of approximately 23 to 33 °C higher than those of the
first comparative example. It should be noted that as a result of investigation of
the combustion characteristics of these diesel fuel compositions, no large differences
were found in the fuel-air mixture formation and flame development processes, ignition
delay and heat release rate in both low and medium load ranges, and there are basically
no differences in macroscopic combustion characteristics.

Particulate comparison
[0031] Next, measurements of the amount of particulate matter (PM) emitted under light load
are shown in Figs. 3 and 4 for the first embodiment and first comparative example.
Particulate matter comprises a soluble organic fraction (SOF), which is a component
soluble in an organic solvent, and insoluble organic fraction (IOF), which is a component
insoluble in an organic solvent and principally comprises soot. The particulate measurements
may be made using the methods described in the literature, for example in F. Black,
SAE Technical Paper 790422. It should be noted that Fig. 3 shows the case where the
fuel injection timing is at a crank angle of degrees before top dead center, and Fig.
4 shows the case where the fuel injection timing is at a crank angle of 0 degrees,
that is to say, at the top dead center. In both of Figs. 3 and 4, the bar indication
A shows the results for the first embodiment and the bar indication
B shows the results for the first comparative example.
[0032] From Figs. 3 and 4 it will be seen that the diesel fuel composition of the first
embodiment exhibits a greatly reduced amount of particulate material, and particularly
of insoluble organic fraction, compared with the diesel fuel composition of the first
comparative example. That is to say, although the first comparative example has a
highly reduced content of aromatic organic compounds and a highly lowered boiling
point, the reduction in particulate emissions is not as effective as that of the first
embodiment.
[0033] To investigate the reason for this contradictory result, analysis of the products
of thermal decomposition of the diesel fuel compositions was carried out.
Analysis of the products of thermal decomposition
[0034] The products of thermal decomposition of two diesel fuels listed in Table 2 and obtained
through a flow reactor were analyzed by a gas chromatography. The operating conditions
of measurement in the flow reactor were as follows: nitrogen gas was used as the carrier
gas, the sample was diluted 50 times by weight, the reaction time (time the gas was
retained in the reaction tube) was 0.65 seconds, and the reaction temperature was
850°C.
[0035] Fig. 5 shows the concentrations of the products (acetylene, propadiene, benzene,
and toluene) obtained by thermal decomposition of the diesel fuel compositions, using
the flow reactor. Acetylene, propadiene, and other hydrocarbons with unsaturated bonds,
and benzene, toluene, and other aromatic hydrocarbons are the substances which are
the origin of the polycyclic aromatic hydrocarbons which are the precursors to particulate
matter.
[0036] From Fig. 5 it is clear that the products of thermal decomposition of the diesel
fuel composition of the first comparative example are produced in two to three times
the quantity of those of the first embodiment. Thus, although the aromatic hydrocarbon
content of the diesel fuel composition of the first comparative example has been greatly
reduced, the substances which are the origin of the polycyclic aromatic hydrocarbons
are produced in large quantities by thermal decomposition, and as a result the effect
of reducing particulate emissions is lost, and if anything there can be an increase.
[0037] In this respect, a more detailed investigation was made of the influence of the presence
or absence or the number of branches in hydrocarbons within a diesel fuel composition
on the substances which are the origin of the polycyclic aromatic hydrocarbons which
are the precursors to particulate matter, taking paraffins as an example.
Analysis of the influence of paraffin molecular structure on particulate generation
(1) Analysis of the effect of paraffin branching structure on the products of thermal
decomposition using a flow reactor
Purpose:
[0038] In this experiment, in order to investigate the influence of paraffin branching structure
within a diesel fuel composition on the generation of polycyclic aromatic hydrocarbon
precursors which are the origin of particulate matter, from the viewpoint of the chemical
properties of the diesel fuel composition, products of thermal decomposition by a
flow reactor were analyzed. A number of simple paraffins with or without branches
and of different numbers of branches were used as examples. Method of measurement:
[0039] Using a flow reactor in the same way as for the thermal decomposition of diesel fuel
compositions described above, measurements were made under the same conditions except
for the reaction temperature. More specifically the measurement conditions were as
follows.
Carrier gas: nitrogen gas
Sample dilution: 50 times by weight
Reaction time: 0.65 seconds
Reaction temperature: 1000°C
[0040] As samples were used hexanes, with six carbon atoms. More specifically, three isomers
were used: n-hexane, 2-methylpentane (i-hexane with one branch), and 2,2-dimethylbutane
(i-hexane with two branches). Results:
[0041] The concentrations of products of thermal decomposition (acetylene, propadiene, benzene,
and toluene) are shown in Fig. 6. From Fig. 6, it will be seen that for each of propadiene,
benzene, and toluene, as the number of branches increases, these substances which
are precursors to polycyclic aromatic hydrocarbons are produced in larger quantities.
For acetylene, on the other hand, it will be seen that the number of branches has
little effect.
(2) Analysis of the influence of the paraffin branching structure on the generation
of soot, using a shock tube
Purpose:
[0042] In this experiment, in order to investigate the influence of paraffin branching structure
within a diesel fuel on the generation of soot, from the viewpoint of the chemical
properties of the diesel fuel composition, the amount of soot generated was measured
in an ideal combustion field (field of spatially uniform and high temperature and
pressure formed instantaneously) in a shock tube. A number of simple paraffins of
different molecular structure were used as fuel. That is to say, the purpose of this
experiment is to simplify the complicated phenomena occurring in a diesel engine,
and prove chemically that the paraffin molecular structure has an effect on the amount
of soot generated.
Experimental method:
[0043] A shock tube is a widely used device in the field of physical chemistry, as described
in the literature (for example, Technopia, World Science Dictionary, published by
Kodansha, Vol. 8, pp. 188-189, and M. Frenklach and S. Taki. A Conceptual Model for
Soot Formation in Pyrolysis of Aromatic Hydrocarbons. Combustion and Flame 49. pp.
275-282, 1983). The shock tube used in this experiment was a stainless steel cylinder
(outer diameter 89.1 mm, inner diameter 78.1 mm), and the lengths of the low pressure
chamber (driven section) and the high pressure chamber (driver section) were 6 m and
3 m respectively.
[0044] In the experiment, first the low pressure chamber and the high pressure chamber were
separated with an aluminum diaphragm, and the low pressure chamber and the high pressure
chamber were evacuated to a vacuum, after which into the low pressure chamber was
introduced as shown in Table 3 a test fuel gas diluted with argon, and the high pressure
chamber was charged with helium as a driver gas, respectively at given pressures.
Next the diaphragm was ruptured with an impact needle or spontaneously under the pressure
of the high pressure chamber, whereby a shock wave was generated. A shock wave (the
incident shock wave) advancing from the diaphragm toward the end wall of the low pressure
chamber at the speed of sound or faster reached the end wall of the low pressure chamber
and was reflexed, becoming a reflected shock wave. Behind this reflected shock wave,
a high temperature field was instantaneously formed (duration approximately 1.5 ms),
and thereby a reaction of the test fuel gas was caused, and soot was generated. It
should be noted that the initial temperature of the reaction field generated by the
reflected shock wave can be easily calculated from a measurement of the velocity of
the incident shock wave into the low pressure chamber.
[0045] The amount of soot generated by the reaction was measured from the transmissivity
of a helium neon laser passing through a pair of optical windows disposed at a distance
of 1 cm from the end wall of the low pressure chamber. That is to say, using the fact
that the transmissivity is reduced since the helium neon laser is attenuated by scattering
by soot particles, the amount of soot can be determined. In this experiment, the benchmark
used to indicate the amount of soot generated is the "soot conversion ratio" (proportion
of the number of carbon atoms which are converted to soot particles to the total number
of carbon atoms in the fuel of initial stage) defined by the well-known expression
(1) from the measurement of the transmissivity of a helium neon laser. (For example,
A. Alexiou and A. Williams. Soot Formation in Shock-Tube Pyrolysis of Toluene, Toluene-Methanol,
Toluene-Ethanol, and Toluene-Oxygen Mixtures. Combustion and Flame 104. pp. 51-65,
1996)

[0046] The soot conversion ratio
t seconds after the start of the reaction can be found, using the transmissivity
T(t) of the helium neon laser measured in the experiment using the well-known expression
(2).

where
- N:
- Avogadro's number
- ρ:
- soot particle density
- λ:
- wavelength of transmitted light
- l:
- optical path length (78.1 mm: internal diameter of shock tube)
- T(t):
- transmissivity at time t
- [C]o:
- initial carbon concentration behind reflected shock wave

- m:
- complex refractive index of soot particles It should be noted that in this experiment
a value of
- E(m)
- = 0.253 was used.
[0047] In this experiment, as paraffins of different molecular structures were used five
hexanes. Table 3 shows the composition of the (test fuel) gas charged in the low pressure
chamber, the initial reaction temperature, the initial reaction pressure, and the
initial carbon concentration behind the reflected shock wave.
[0048] It should be noted that the temperature behind the reflected shock wave (initial
reaction temperature) was varied by adjusting the pressure of the propulsion gas (helium)
charged in the high pressure chamber. In Table 3, in the composition of the gas charged
in the low pressure chamber, the proportions of paraffin and oxygen are in a chemical
equivalence ratio of 10, and this equivalence ratio is the condition corresponding
to the excessively rich mixture portion in a diesel engine.

Results:
[0049] The results are shown in Figs. 7 to 11. In Figs. 7 to 11, the horizontal axis represents
the temperature (initial reaction temperature) behind the reflected shock wave, and
the vertical axis represents the soot conversion ratio 1 millisecond after the start
of the reaction. All the results exhibit characteristics which reach a maximum soot
conversion ratio at a particular temperature, that is to say, bell curves.
[0050] Fig. 12 shows a comparison of the peak values of the bell curves shown in Figs. 7
to 11. Compared with the n-hexane (zero branches) in experiment number 1, the methylpentane
(i-hexane with one branch) in experiments number 2 and 3, and the dimethylbutane (i-hexane
with two branches) in experiments number 4 and 5 exhibit progressively higher values
of the soot conversion ratio (soot production capacity). That is to say, the soot
production capacity increases as the number of branches increases. From comparisons
of experiments number 2 and 3 and experiments number 4 and 5, however, the position
of the branches has only a small effect on the soot production capacity.
[0051] From the above it is seen that:
(1) Soot is more easily generated from branching paraffins than from unbranching paraffins;
and
(2) The soot production capacity is little influenced by the position of the branches
within the paraffin, and is largely determined by the number of branches.
[0052] Thus, the influence over the production of soot exerted by the molecular structure
of paraffins in a diesel fuel composition has been chemically confirmed by the above
experiments, where the effects of complicated phenomena inside the diesel engine have
been eliminated.