BACKGROUND OF THE INVENTION
1. Field of the Invention
[0001] The present invention relates to a method and a device for supplying fuel to an internal
combustion engine. More specifically, the invention relates to a method and a device
in which a liquid fuel supplied to the engine is in a supercritical state.
2. Description of the Related Art
[0002] In general, a fuel supply system for an internal combustion engine is required to
supply liquid fuel to combustion chambers of the engine in the form of a very fine
mist. Especially, in a direct cylinder injection system for injecting fuel into the
combustion chamber directly, such as the injection system of a diesel engine, the
size of particles of the injected fuel largely affects the performance of the engine.
In the direct cylinder injection system, the combustion of the fuel in the combustion
chamber, and thus the performance of the engine can be largely improved by reducing
the size of the particles of the injected fuel.
[0003] It is considered that a high pressure fuel injection, in which fuel is injected from
the fuel injection valve at a very high pressure, is effective in order to reduce
the size of the particles of the injected fuel. Therefore, in recent fuel injection
systems, the fuel injection pressure is set at a very high value in order to satisfy
the requirement for low exhaust gas emission and low fuel consumption. For example,
some of the fuel injection systems for diesel engines use a fuel injection pressure
as high as more than 50 MPa (500 atm) to generate very fine particles of injected
fuel in the combustion chamber.
[0004] However, in the high pressure fuel injection system a fuel pump which is capable
of pressurizing the fuel to a very high pressure is required. Since the high pressure
fuel pump is very expensive, this increases the cost of whole fuel injection system.
Further, in the high pressure fuel pump, the clearances between the sliding parts
must be small in order to prevent the high pressure fuel from leaking. This tends
to cause wear of the sliding parts and lowers the reliability of the pump.
SUMMARY OF THE INVENTION
[0005] In view of the problems in the related art as set forth above, the object of the
present invention is to provide a method and a device for supplying fuel to internal
combustion engine which is capable of improving combustion of an internal combustion
engine without using a very high fuel injection pressure.
[0006] This object is achieved by a method for supplying fuel to an internal combustion
engine, comprising a step for adjusting temperature and pressure of liquid fuel so
that at least some of the components of the fuel are in a supercritical state, and
a step for supplying the fuel in the supercritical state to a combustion chamber of
an internal combustion engine.
[0007] In this aspect of the present invention, the liquid fuel is in a supercritical state,
and this supercritical state fuel is supplied to the combustion chamber. In the supercritical
state, both the temperature and the pressure of the liquid fuel is higher than the
critical values. In this condition, the liquid fuel becomes a gaseous fluid which
has a very high density and has physical properties very near to those of a liquid.
However, since the supercritical fluid maintains its gaseous characteristics at the
same time, when the liquid fuel in the supercritical state is injected from the fuel
injection valve into the combustion chamber, it diffuses throughout the entire combustion
chamber and forms an extremely fine mist of fuel.
[0008] As explained later, the critical pressure of liquid fuel is relatively low (for example,
in case of diesel fuel, the critical pressure is generally much lower than 10 MPa).
Therefore, by injecting fuel in the supercritical state, it is possible to improve
the combustion of engine by forming a very fine mist of fuel in the combustion chamber
without raising the fuel injection pressure to a very high level.
[0009] According to another aspect of the present invention, there is provided a method
for supplying fuel to an internal combustion engine for a vehicle comprising a step
for reforming liquid fuel by adjusting the temperature and pressure of the fuel on
the vehicle in such a manner that at least some of the components of the fuel are
in a supercritical state and a step for supplying the fuel, after it is reformed,
to a combustion chamber of an internal combustion engine.
[0010] In this aspect of the invention, liquid fuel is reformed on the vehicle by bringing
the fuel into the supercritical state. Liquid fuel, such as diesel fuel, contains
a relatively large amount of heavy components such as normal paraffin components and
aromatic hydrocarbons having large molecular weights. These components, when burned
in the combustion chamber, form particulate matter (carbon particles) in the exhaust
gas. It is found that these heavy normal paraffin components are cracked at a relatively
low temperature and produce light components such as normal paraffin having low molecular
weight when the fuel is kept in the supercritical state. Therefore, in this aspect
of the invention, liquid fuel containing a large amount of heavy components is reformed
on the vehicle, and the reformed fuel which contains a large amount of light components
is supplied to the combustion chamber of the engine. Therefore, the combustion of
the engine is improved.
[0011] The reformed fuel may be supplied to the engine in the supercritical state. In this
case, the combustion of the engine is further improved due to the improvement in the
atomization of the fuel and the increase in the amount of the light components in
the supplied fuel.
[0012] Further, in the above aspects of the invention, when diesel fuel is used, an oxygen-containing
substance may be added to the fuel before it reaches the supercritical state. In this
specification, the term "oxygen-containing substance" means a substance such as water
or methanol which contains oxygen or a hydroxyl group. When the fuel containing the
oxygen-containing substance is burned, production of aromatic hydrocarbons during
the combustion is suppressed and, thereby, the combustion is improved. Further, when
the fuel containing an oxygen-containing substance is reformed in the supercritical
state, production of aromatic hydrocarbons is suppressed during the cracking of heavy
normal paraffin. Therefore, the combustion of the engine is improved.
[0013] In another aspect of the present invention, there is provided a device for supplying
fuel to an internal combustion engine comprising a fuel tank for storing liquid fuel,
a fuel injection valve for injecting the fuel supplied from the fuel tank into a combustion
chamber of an internal combustion engine, supercritical state generating means disposed
on a fuel supply path from the fuel tank to the fuel injection valve for adjusting
the temperature and pressure of the fuel so that at least some of the components of
the fuel reaches a supercritical state.
[0014] According to this aspect of the invention, liquid fuel reaches a supercritical state
due to the supercritical state generating means before it is injected into the combustion
chamber. Therefore, the fuel in the supercritical state, or the fuel reformed by keeping
it in a supercritical state is supplied to the combustion chamber of the engine. The
supercritical state generating means may include a pressurizing means such as a pump
for raising the pressure of the fuel to higher than the critical pressure and heating
means such as a heater for raising the temperature of fuel to above the critical temperature.
[0015] According to another aspect of the present invention, there is provided a method
for supplying diesel fuel to an internal combustion engine comprising a step for reforming
diesel fuel by keeping the fuel in the conditions where the temperature is higher
than 400°C and the pressure is higher than 1.5 MPa and a step for supplying the fuel,
after it is reformed, to the engine.
[0016] In this aspect of the invention, diesel fuel (gas oil) is reformed by keeping it
in the conditions where the temperature is higher than 400°C and the pressure is higher
than 1.5 MPa. It is found that in these conditions, the heavy normal paraffin components
in diesel fuel are cracked and produce lighter normal paraffin components. Further,
the specific gravity and kinematic viscosity of the diesel fuel are largely lowered
without changing the cetane number of the fuel by reforming the diesel fuel in these
conditions. Therefore, by adding more than 1 percent weight of the reformed fuel to
normal diesel fuel, the atomization of the fuel when injected into the combustion
chamber is improved.
[0017] According to another aspect of the present invention, there is provided a method
for supplying diesel fuel to an internal combustion engine comprising a step for reforming
diesel fuel by keeping the fuel in the conditions where the temperature is between
400°C and 550°C and the pressure is higher than 1.5 MPa and a step for supplying the
fuel, after it is reformed, to the engine.
[0018] In this aspect of the invention, diesel fuel (gas oil) is reformed by keeping it
in the conditions where the temperature is between 400°C and 550°C and the pressure
is higher than 1.5 MPa. It was found that in these conditions, heavy normal paraffin
components in the diesel fuel are cracked and produce lighter normal paraffin components
without producing heavy alkylbenzene components. Also in this case, more than 1 percent
by weight of the reformed fuel may be added to a normal diesel fuel.
BRIEF DESCRIPTION OF THE DRAWINGS
[0019] The present invention will be better understood from the description as set forth
hereinafter, with reference to the accompanying drawings in which:
Fig. 1 schematically illustrates the general configuration of an embodiment of the
present invention;
Fig. 2 schematically illustrates the general configuration of an embodiment of the
supercritical fuel injection pump;
Fig. 3 illustrates the general configuration of another embodiment of the present
invention;
Fig. 4 is a graph showing the critical pressure and the critical temperature of the
components contained in diesel fuel; and
Figs. 5 through 9 are graphs and tables illustrating the result of the reforming of
diesel fuel in the supercritical state.
DESCRIPTION OF THE PREFERRED EMBODIMENT
[0020] Hereinafter, embodiments of the present invention will be explained in detail with
reference to the accompanying drawings. However, before explaining the embodiments,
the supercritical state of liquid fuel will be explained.
[0021] The supercritical state is a state achieved by heating a substance above the critical
temperature under a pressure higher than the critical pressure. When a liquid substance
is pressurized and heated to the supercritical state, the phase of the substance changes
from liquid to gas. However, gas in the supercritical state has a very high density
and, therefore, it shows physical characteristics very similar to liquid. Namely,
when liquid is in the supercritical state, it becomes a supercritical fluid having
physical characteristics between those of liquid and gas. Since the supercritical
fluid has a very high density, it has a large energy and shows a unique behavior.
[0022] For example, when the supercritical fuel fluid is injected from the fuel injection
valve into the combustion chamber which has a pressure and temperature lower than
that of the supercritical state, a mist of fuel having particle sizes much smaller
than those formed by the high pressure fuel injection is uniformly formed in the combustion
chamber. When the supercritical fuel fluid is injected from the fuel injection valve,
the temperature and/or pressure of the fluid becomes lower than the critical values.
This causes the state of the fuel fluid to change from a supercritical to a subcritical
in which the temperature or the pressure of the fuel fluid is lower than the critical
value. Therefore, a part of the fuel fluid injected from the fuel injection valve
changes to a normal gas state and diffuses throughout the entire combustion chamber.
Further, the remaining part of the fuel fluid returns to a liquid state and forms
a mist of fuel having very small particle size in the combustion chamber. Since the
particles of fuel in the mist are formed by a change of phase (i.e., condensing),
the size of the particles are very small compared to the size of the particles mechanically
formed by high pressure fuel injection. In addition to that, since the injected supercritical
fuel fluid, which has the characteristics of a gas, diffuses throughout the entire
combustion chamber instantaneously, the formation of fine fuel particles by the above
phase change (condensing) occurs simultaneously in the entire combustion chamber.
Therefore, a very fine mist of fuel is uniformly formed in the entire combustion chamber.
[0023] Further, the critical pressure of diesel fuel is relatively low (for example, generally
lower than 10 MPa). This means that, by injecting fuel in the supercritical state,
a uniform fine mist of fuel having a much smaller particle size compared to those
in the high pressure fuel injection is obtained with much lower fuel pressure.
[0024] Further, each of the fuel particles formed by the injection of supercritical fuel
fluid have a high energy level due to latent heat released by the condensation and,
therefore, readily react with oxygen. In addition to that, since the fine mist of
fuel is uniformly formed in the entire combustion chamber by the injection of supercritical
fuel fluid, sufficient oxygen is supplied to each fuel particle which is, as explained
above, highly reactive. Therefore, the fuel in the combustion chamber is readily ignited
and is burned completely, i.e., the combustion of the engine is largely improved and,
thereby, both the exhaust gas emission and fuel consumption of the engine are reduced
by the improvement of the combustion.
[0025] Fig. 4 is a graph illustrating the pressure and temperature conditions required to
make diesel fuel reach the supercritical state. Generally speaking, diesel fuel is
a mixture of normal paraffin (n-paraffin) having 11 to 20 carbon atoms and aromatic
hydrocarbons (alkylbenzene) having 10 to 22 carbon atoms. Since the critical pressure
and the critical temperature depend on the substance, each component of diesel fuel
has different critical pressure and temperature.
[0026] Fig. 4 illustrates the change in the critical pressure and temperature of n-paraffin
and alkylbenzene in accordance with the difference in the number of carbon atoms.
The vertical axis and the horizontal axis in Fig. 4 represent the critical pressure
and the critical temperature of the respective components. As shown in Fig. 4, in
general, the critical pressure becomes lower as the number of carbon atoms is larger,
and the critical temperature becomes higher as the number of carbon atoms is larger.
Further, when the n-paraffin and the alkylbenzene having same number of carbon atoms
are compared, both the critical pressure and the critical temperature of the n-paraffin
are generally lower than the same of the alkylbenzene.
[0027] The hatched portions A and B in Fig. 4 indicate the range of the numbers of carbon
atoms of the n-paraffin components and the alkylbenzene components usually composing
diesel fuel. As can be seen from Fig. 4, it is required that both the pressure and
the temperature of the diesel fuel must be in the region SC1 in Fig. 4 in order to
make all the components in diesel fuel reach the supercritical state. The region SC1
represents a pressure more than 3 to 6 MPa and a temperature more than 400 to 500°C.
However, in the actual operation, it is found that the improvement of the combustion
of the engine can be achieved even when only some of the components in diesel fuel
reach a supercritical state. Therefore, even in a pressure/temperature condition in
which only some of the n-paraffin components and the alkylbenzene components are in
the supercritical state, for example, when the pressure is more than 1 MPa and the
temperature is more than 300°C, an improvement in the combustion of the engine can
be achieved. As explained before, the critical pressure becomes lower as the number
of carbon atoms in the components increase while the critical temperature becomes
higher as the number of carbon atoms in the components increase.
[0028] Therefore, if only some of the components of diesel fuel should reach the supercritical
state, the pressure can be lowered when the temperature is maintained at high level.
[0029] As explained above, combustion of the engine is improved, with a much lower fuel
injection pressure compared to that of the high pressure fuel injection system, by
injecting diesel fuel into combustion chambers in the supercritical state. Therefore,
by injecting diesel fuel in the supercritical state, the pressure rating of the fuel
injection pump can be largely lowered and, thereby, the cost of fuel injection pump
can be lowered and the reliability thereof improved.
[0030] Next, reforming of fuel by a supercritical treatment is explained.
[0031] It is also found that heavy components in liquid fuel are converted to lighter components,
i.e., reforming of fuel is performed, by keeping liquid fuel in the supercritical
state for a certain time (i.e., a supercritical treatment).
[0032] Fig. 5 shows the result of reforming of diesel fuel by the supercritical treatment.
In Fig. 5, the vertical axis represents the change in the concentrations of the n-paraffin
components in diesel fuel caused by the supercritical treatment, and the horizontal
axis represents the number of carbon atoms in the respective n-paraffin components.
Fig. 5 shows the case where diesel fuel is held at the temperature between 400 and
500°C and the pressure between 4 and 5 MPa for about 20 minutes. As can be seen from
Fig. 5, the concentrations of heavy n-paraffin components (number of carbon atoms
is 13 or more) decrease and, at the same time, the concentrations of light n-paraffin
components (number of carbon atoms is 12 or less) increase due to the supercritical
treatment. This means that a part of the heavy components in diesel fuel are converted
to the lighter components, i.e., diesel fuel is reformed by the supercritical treatment.
Further, it is found that the increase in the light n-paraffin components becomes
larger as the pressure and temperature in the supercritical treatment are higher and
the time of the supercritical treatment is longer.
[0033] According to experiment, it was found that a pressure more than 1.5 MPa is preferable
to reform the heavy components in diesel fuel. Fig. 7 shows the results of experiments
in which diesel fuel is treated at various temperature and time under the pressure
1.5 MPa. In Fig. 7, the letter C represents the case where no change of the concentrations
of the components of the diesel fuel occurred by the treatment, the letter B represents
the case where the amount of heavy n-paraffin components is slightly decreased by
the treatment and the letter A represents the case where the amount of heavy n-paraffin
components is decreased by the treatment. As can be seen from Fig. 7, when the pressure
is kept at 1.5 MPa, diesel fuel is reformed (i.e., the heavy components in the diesel
fuel decreases) when the temperature is more than 400°C. Further, as can be seen from
Fig. 7, as the temperature becomes higher, the time required for reducing the heavy
components becomes shorter. For example, in Fig. 7, when the temperature is 400°C,
a 120 minutes treatment time is required to reduce the heavy components. However,
it takes less than 1 minute when the temperature is higher than 475°C.
[0034] As explained above, in order to reduce the heavy components in the diesel fuel, it
is preferable to raise the temperature and pressure as high as possible. However considering
the reliability of the elements in the reforming device and the seal problems, it
is preferable to use a temperature lower than 600°C and a pressure lower than 30 MPa.
[0035] Further, it was also found that light alkylbenzene components are produced by the
decomposition of heavy n-paraffin components and the concentrations of alkylbenzene
components increase when the temperature of the supercritical treatment is high. Fig.
6 shows the change in the concentrations of alkylbenzene components in the same diesel
fuel as Fig. 5 due to the supercritical treatment where the diesel fuel is kept at
600°C and 5 MPa for about 20 minutes. As can be seen from Fig. 6, when the temperature
in the supercritical treatment is high, light alkylbenzene components (the number
of carbon atoms is 12 or less) increase due to the conversion of heavy n-paraffin
components to light alkylbenzene components.
[0036] Generally, particulate matter in the exhaust gas of the engine increases as the alkylbenzene
components or heavy n-paraffin components in diesel fuel increase. Especially, the
alkylbenzene components having the number of carbon atoms more than 12 increases the
particulate matter in the exhaust gas. Therefore, it is not preferable that the heavy
alkylbenzene components in diesel fuel increase by the supercritical reforming treatment.
[0037] Fig. 8 shows the results of experiments in which diesel fuel is treated at various
temperature and time under a pressure of 5 MPa. In Fig. 8, the letter C represents
the case where the concentrations of the heavy alkylbenzene components of the diesel
fuel are increased by the treatment, the letter B represents the case where the heavy
alkylbenzene components are slightly increased by the treatment and the letter A represents
the case where the heavy alkylbenzene components are not increased by the treatment.
As can be seen from Fig. 8, the heavy alkylbenzene components increases when the temperature
is higher than 550°C even the treatment time is 1 minute. However, as can be seen
from Fig. 8, as the temperature becomes lower, the treatment time which does not increase
the heavy alkylbenzene components becomes longer.
[0038] Therefore, when the pressure is higher than 1.5 MPa, and the temperature between
400°C and 550°C, the conditions where the heavy n-paraffin components reform and,
at the same time, the heavy alkylbenzene components do not increase can be found.
[0039] Further, in order to suppress the production of alkylbenzene during the supercritical
reforming treatment, it is effective to add an oxygen-containing substance such as
water and methanol to the diesel fuel to be treated. By applying the supercritical
reforming treatment to diesel fuel after adding water or methanol by several percent
to about twenty percent by weight, the conversion of decomposed heavy n-paraffin components
to alkylbenzene components is suppressed. Further, it is known that small amounts
of alkylbenzene components are produced by the combustion of n-paraffin components
in diesel fuel. However, by adding the oxygen-containing substance to diesel fuel,
the production of alkylbenzene components during the combustion of diesel fuel can
be suppressed and, thus, the amount of the particulate matter in the exhaust gas can
be reduced.
[0040] Fig. 9 shows changes in the physical properties of diesel fuel caused by the supercritical
treatment. Fig. 9 shows the physical properties of a normal diesel fuel (a gas oil
which complies with JIS JTD-5) and the properties of the fuel obtained by reforming
the same diesel fuel in the condition where the pressure is 5 MPa and the temperature
is between 400 and 550°C. As can be seen from Fig. 9, the kinematic viscosity and
flash point are lowered by the supercritical treatment while maintaining the same
cetane number. This means that, when the reformed fuel is injected into the combustion
chamber, it forms a fine mist (due to the lower kinematic viscosity) which readily
ignites (due to the lower flash point) in the combustion chamber. Further, the fact
that the reformed fuel has a lower initial boiling point and a lower flash point means
that the reformed fuel has a higher volatility than normal diesel fuel while maintaining
the same cetane number. Therefore, the reformed fuel can be used as an additive for
the normal diesel fuel to promote initial combustion in the combustion chamber. When
used as an additive for normal diesel fuel to promote the initial combustion, the
concentration of the reformed fuel in the mixture should be more than 1 percent by
weight, preferably more than 5 percent by weight.
[0041] Next, an embodiment of a fuel injection device for the injection of liquid fuel in
the supercritical state into the combustion chamber of the engine is explained. Fig.
1 schematically illustrates the general configuration of a fuel injection device according
to the present invention.
[0042] In Fig. 1, reference numeral 1 designates a diesel engine, 2 designates a fuel injection
valve which injects diesel fuel in the supercritical state into the respective combustion
chambers of the engine 1. 11 in Fig. 1 is a fuel storage tank for storing diesel fuel
of the engine and, 13 is a feed pump for supplying diesel fuel in the storage tank
11 to a injection fuel tank 15.
[0043] Numeral 17 in Fig. 1 is a critical pressure pump which feeds the diesel fuel from
the tank 15 to supercritical fuel injection pump 19 at a pressure higher than the
critical pressure. Numeral 18 is a supercritical state generating device which includes
a heating device such as an electric heater 18b for heating the diesel fuel supplied
from supercritical fuel injection pump 19 to the fuel injection valve 2 so that the
temperature of the diesel fuel becomes higher than the critical temperature.
[0044] The diesel fuel in the injection fuel tank is pressurized by the critical pressure
pump to, for example, 3 to 6 MPa and flows into a heating chamber 18a in the supercritical
state generating device 18 through a fuel passage 19h disposed in the body 19a of
the supercritical fuel injection pump 19, as explained later. Then, the fuel in the
heating chamber 18a is heated by the heater 18b to a temperature higher than the critical
temperature (for example, 400 to 500°C) and reaches the supercritical state. When
a fuel injection timing occurs, the diesel fuel in the heating chamber 18a is further
pressurized by a plunger 19b of the supercritical fuel injection pump 19. When the
pressure in the heating chamber 18a becomes higher than an opening pressure of the
fuel injection valve 2, fuel in the supercritical state is injected from the fuel
injection valve 2 and forms an extremely fine uniform fuel mist in the combustion
chamber of the engine 1.
[0045] Fig. 2 shows a general construction of the supercritical fuel injection pump 19 in
Fig. 1.
[0046] In Fig. 19, 19d is a cylinder of the supercritical fuel injection pump 19, 19c is
a solenoid actuator which is mounted on the cylinder 19d. 19a is a spool disposed
in the cylinder 19d. Driven by the solenoid actuator 19c, the spool 19a slides within
the cylinder 19d. 19b is a plunger which is driven by a camshaft (not shown) of the
engine 1 and reciprocates within the cylinder. 19e in Fig. 1 is a pressure chamber
defined in the cylinder 19d by the spool 19a and the plunger 19b. The stroke of the
plunger is adjusted by a governor (not shown) in accordance with the load of the engine
1. During the downward motion of the plunger 19b, the spool 19a is held at a downward
position as shown in Fig. 2 by the solenoid 19c. This causes the fuel from the critical
pressure pump 17 to flow directly into the heating chamber 18a of the supercritical
state generating device 18 through the pipe 21, the port 21a of the cylinder 19d,
the fuel passage 19h of the spool 19a, the port 24a and the pipe 24. Fuel is also
fed from the critical pressure pump 17 to the pressure chamber 19e through the pipes
22 and 22a. After the plunger 19b reaches a position of the port 23a during its downward
stroke, excess fuel is returned to the storage tank 11 through the port 23a and the
return pipe 23. The return pipe 23 is provided with a cooling water jacket 23b for
cooling the fuel flowing through the pipe 23.
[0047] When the upward stroke of the plunger 19b starts, the ports 23a and 22a are closed
by the plunger 19b and the pressure of the fuel in the pressure chamber 19e increases.
In this condition, when a fuel injection timing occurs, the spool 19a is moved to
an upward position by the solenoid 19c. At the upward position of the spool 19a, the
fuel passage 19h is closed, and another fuel passage 19j is connected to the port
24a. Therefore, the fuel in the pressure chamber 19e which is pressurized by the upward
motion of the plunger 19b flows into the heating chamber 18a of the supercritical
state generating device 18. This causes the pressure in the heating chamber 18a to
increase further. The passage 19j is provided with check valve 19k for preventing
the backflow of the pressurized fuel from the heating chamber 18a to the pressure
chamber 19e.
[0048] When the pressure of the fuel in the heating chamber becomes higher than the valve
opening pressure of the fuel injection valve 2 during the upward motion of the plunger
19b, the supercritical state fuel in the chamber 18a is injected from the fuel injection
valve 2 into the combustion chamber of the engine 1. After the required amount of
the fuel is injected, the plunger 19b starts the downward stroke. This lowers the
pressure of the fuel in the heating chamber 18a, and when the pressure in the chamber
18a becomes lower than the opening pressure of the fuel injection valve 2, the fuel
injection stops. In this condition, since the check valve 19k closes, the pressure
in the heating chamber 18a is kept higher than the critical pressure and, thereby
the fuel in the heating chamber is kept in the supercritical state. Then, the spool
19a is moved to the downward position as shown in Fig. 2, and next fuel injection
cycle starts.
[0049] The time the fuel resides in the heating chamber 18a can be arbitrary set by selecting
the volume of the heating chamber 18a. Therefore, the residence time can be set long
enough to assure that the fuel is heated to the temperature higher than the critical
temperature by the heater 18b. As explained above, a liquid fuel in the supercritical
state can be injected into the combustion chamber of the engine by the fuel injection
system in Figs. 1 and 2.
[0050] It is preferable to set the opening pressure of the fuel injection valve 2 and the
temperature in the heating chamber 18a higher than the pressure and the temperature
which can make all the components in the fuel reach the supercritical state (for example,
a temperature higher than 500°C and a pressure higher than 6 MPa. However, as explained
before, even if the temperature and pressure conditions are set so that only some
of the components in the fuel reach the supercritical state, it is possible to form
a very fine mist in the combustion chamber. Further, the oxygen-containing substance
such as water or methanol may be added to the fuel in the tank 11 in order to suppress
the formation of alkylbenzene components by the combustion of the fuel.
[0051] Next, an example of the device for reforming liquid fuel by applying the supercritical
treatment is explained with reference to Fig. 3.
[0052] Fig. 3 shows a general configuration of the device which reforms the fuel in the
storage tank 11 by the supercritical treatment. In Fig. 3 reference numerals the same
as those in Figs. 1 and 2 designate the same elements.
[0053] In the embodiment in Fig. 3, a supercritical reformer 31 and a second critical pressure
pump 33 which feeds the fuel in the tank 11 to the supercritical reformer 31 are provided.
Further, a reformed fuel tank 35 which stores the reformed fuel instead of the fuel
injection tank 15 in Fig. 1 is provided.
[0054] In this embodiment, the second critical pressure pump 33 feeds the diesel fuel to
the supercritical reformer 31 at a pressure higher than 1.5 MPa. The supercritical
reformer 31 is provided with a heater 31a and a heating passage heating passage 31b.
The fuel is heated by the heater 31a to a temperature higher than the critical temperature
when it flows through the heating passage 31b, and reaches the supercritical state.
The flow velocity of the fuel in the heating passage 31b, i.e., the time the fuel
resides in the passage 31b is controlled by a flow control valve 37. In this embodiment,
the capacity of the heater 31a and the flow of the fuel in the supercritical reformer
31 is selected so that the fuel is held within the heating passage 31b for about 1
to 20 minutes at a temperature between 400°C and 550°C. By this arrangement, the fuel
is reformed in the supercritical state when it flows through the heating passage 31b,
and the reformed fuel flows into the reformed fuel tank 35.
[0055] Further, the reformed fuel in the reformed fuel tank 35 is made the supercritical
state again by the critical pressure pump 17, supercritical fuel injection pump 19
and supercritical state generating device 18 before it is injected from fuel injection
valve 2 into the combustion chamber of the engine. The constructions and the functions
of these devices are the same as those explained in the embodiment in Fig. 1, and
detailed explanation is not given here.
[0056] According to the present embodiment, all the devices required for reforming the fuel
are disposed on the fuel path between the fuel storage tank 11 and the fuel injection
valve 2. Therefore, when the system in Fig. 2 is applied to an engine for a vehicle,
normal liquid fuel supplied to the vehicle can be reformed on the vehicle. This feature
is especially advantageous because a normal fuel can be supplied to the vehicle and
a facility for supplying the special (reformed) fuel to the vehicle is not required.
[0057] The reformed fuel is injected from the fuel injection valve in the supercritical
state in this embodiment. However, the combustion of the engine is largely improved
even if the reformed fuel is injected in a normal state (i.e., at a lower fuel injection
pressure). Further, though the fuel flows through the supercritical reformer 31, and
reformed contiguously in the above embodiment, a certain amount of the fuel may be
reformed at a time. In this case, a shutoff valve which may be opened and closed by
a timer is provided instead of flow control valve 37 to hold a certain amount of the
fuel within the supercritical reformer 31 for a predetermined time. After the fuel
in the supercritical reformer 31 is reformed, the shutoff valve is opened to drain
the reformed fuel in the reformer 31 to the reformed fuel tank 35. Further, the oxygen-containing
substance such as water or ethanol may be added to the fuel in the storage tank 11
also in this embodiment in order to suppress the production of alkylbenzene components
during the reforming and combustion of the reformed fuel.
[0058] As explained above, according to the present invention, the combustion in the combustion
chamber of the engine is improved and, thereby, the exhaust gas emission and the fuel
consumption of the engine are reduced at the same time by injecting and/or reforming
liquid fuel in the supercritical state without using a very high fuel injection pressure.
[0059] According to the present invention, the state of a liquid fuel such as diesel fuel
is made a supercritical state by raising the pressure and the temperature of the fuel
above the critical pressure and temperature. Then, the fuel is injected from the fuel
injection valve into the combustion chamber of the engine in the supercritical state.
When the fuel in the supercritical state is injected into the combustion chamber of
the engine, it forms an extremely fine uniform mist in the entire combustion chamber.
Therefore, the combustion of the engine is largely improved.
1. A method for supplying fuel to an internal combustion engine comprising:
a step for adjusting a temperature and a pressure of liquid fuel so that at least
some of the components of the fuel reach a supercritical state; and
a step for supplying the fuel in the supercritical state to a combustion chamber of
the internal combustion engine.
2. A method for supplying fuel to an internal combustion engine for vehicle comprising:
a step for reforming liquid fuel by adjusting temperature and pressure of the fuel
on the vehicle in such a manner that at least some of the components of the fuel reach
a supercritical state; and
a step for supplying the fuel, after it is reformed, to a combustion chamber of the
internal combustion engine.
3. A method according to claim 2, wherein the fuel is supplied to the combustion chamber
of the internal combustion engine in a supercritical state.
4. A method according to claim 1, wherein said internal combustion engine is a diesel
engine, and said liquid fuel is diesel fuel.
5. A method according to claim 2, wherein said internal combustion engine is a diesel
engine, and said liquid fuel is diesel fuel.
6. A method according to claim 3, wherein said internal combustion engine is a diesel
engine, and said liquid fuel is diesel fuel.
7. A method according to claim 4, further comprising a step for adding an oxygen-containing
substance to the fuel before it reaches the supercritical state.
8. A method according to claim 5, further comprising a step for adding an oxygen-containing
substance to the fuel before it reaches the supercritical state.
9. A method according to claim 6, further comprising a step for adding an oxygen-containing
substance to the fuel before it reaches the supercritical state.
10. A device for supplying fuel to an internal combustion engine comprising:
a fuel tank for storing liquid fuel;
a fuel injection valve for injecting the fuel supplied from the fuel tank into a combustion
chamber of an internal combustion engine;
supercritical state generating means disposed on a fuel supply path from the fuel
tank to the fuel injection valve for adjusting a temperature and a pressure of the
fuel so that at least some of the components of the fuel reach a supercritical state.
11. A device according to claim 10, wherein said supercritical state generating means
includes a pressurizing means for raising the pressure of the fuel to a predetermined
pressure and a heating means for raising the temperature of the fuel to a predetermined
temperature.
12. A method for supplying diesel fuel to an internal combustion engine comprising:
a step for reforming diesel fuel by keeping the fuel in the condition where the temperature
is higher than 400°C and the pressure is higher than 1.5 MPa; and
a step for supplying the fuel, after it is reformed, to the engine.
13. A method for supplying diesel fuel to an internal combustion engine comprising:
a step for reforming diesel fuel by keeping the fuel in the condition where the temperature
is between 400°C and 550°C and the pressure is higher than 1.5 MPa; and
a step for supplying the fuel, after it is reformed, to the engine.
14. A method for supplying diesel fuel to an internal combustion engine comprising:
a step for reforming diesel fuel by keeping the fuel in the condition where the temperature
is higher than 400°C and the pressure is higher than 1.5 MPa;
a step for mixing the reformed diesel fuel with diesel fuel not reformed so that the
concentration of the reformed diesel oil in the mixture is between 1 percent and 30
percent by weight; and
a step for supplying said mixture to the engine.
15. A method for supplying diesel fuel to an internal combustion engine comprising:
a step for reforming diesel fuel by keeping the fuel in the condition where the temperature
is between 400°C and 550°C and the pressure is higher than 1.5 MPa;
a step for mixing the reformed diesel fuel with diesel fuel not reformed so that the
concentration of the reformed diesel oil in the mixture is at least 1 percent by weight;
and
a step for supplying said mixture to the engine.
16. A mixture of diesel fuel and a reformed fuel, wherein said reformed fuel is made by
keeping diesel fuel in the condition where the temperature is higher than 400°C and
the pressure is higher than 1.5 MPa, and said mixture contains said reformed fuel
at least 1 percent by weight.
17. A mixture of diesel fuel and a reformed fuel, wherein said reformed fuel is made by
keeping diesel fuel in the condition where the temperature is between 400°C and 550°C
and the pressure is higher than 1.5 MPa, and said mixture contains said reformed fuel
at least 1 percent by weight.
18. A method for reforming diesel fuel comprising a step for keeping the diesel fuel in
the condition where the temperature is higher than 400°C and the pressure is higher
than 1.5 MPa.
19. A method for reforming diesel fuel comprising a step for keeping the diesel fuel in
the condition where the temperature is between 400°C and 550°C and the pressure is
higher than 1.5 MPa.