Vapor fuel processing system having canister for absorbing vapor fuel contained in fuel tank

Information

  • Patent Grant
  • 6394074
  • Patent Number
    6,394,074
  • Date Filed
    Thursday, October 18, 2001
    23 years ago
  • Date Issued
    Tuesday, May 28, 2002
    22 years ago
Abstract
A fuel pump suctions fuel from a fuel tank and discharges it into a pressure tank. Then, the fuel pump suctions the fuel from the pressure tank and pressurizes it. Then, the fuel pump discharges the pressurized fuel toward an engine side through a fuel discharge pipeline. A pressure control valve is opened to communicate an inside of the fuel tank and an inside of the pressure tank when a pressure in the pressure tank becomes equal to or greater than a predetermined pressure. A canister receives activated carbons for absorbing vapor fuel from the fuel tank. A pressurizing pump suctions the vapor fuel from the canister and pressurizes it. The pressurized vapor fuel is then discharged from the pressurizing pump into the pressure tank, so that the vapor fuel is dissolved into the fuel in the pressure tank.
Description




CROSS REFERENCE TO RELATED APPLICATION




This application is based on and incorporates herein by reference Japanese Patent Application No. 2000-320835 filed on Oct. 20, 2000.




BACKGROUND OF THE INVENTION




1. Field of the Invention




The present invention relates to a vapor fuel processing system for dissolving vapor fuel, which is generated in a fuel tank and is absorbed by a canister, into liquid fuel received in the fuel tank.




2. Description of Related Art




In a previously proposed vapor fuel processing system, vapor fuel generated in the fuel tank is absorbed by activated carbons received within a canister and is discharged into an intake air pipeline of an intake air system that supplies intake air to an engine, so that the vapor fuel discharged into the intake air pipeline is combusted in the engine. However, in this system, a deviation in an air-fuel ratio occurs due to the vapor fuel discharged into the intake air pipeline. This may result in an increase in the amount of noxious components contained in exhaust gas of the vehicle. This is not favorable for satisfying various emission standards, such as the SULEV standard. Thus, it is desirable to reduce the amount of the vapor fuel discharged into the intake air pipeline.




Furthermore, there is a strong demand for improving fuel consumption of vehicles. In an engine that can achieve improved fuel consumption, a negative pressure of intake air is reduced due to a reduction in a pumping loss and an increase in fuel combustion in a lean fuel range. In the engine that has the reduced negative pressure of the intake air, the amount of the vapor fuel, which is absorbed by the canister and is then removed from the canister into the intake air pipeline through use of the negative pressure of the intake air, is reduced.




The system that discharges the vapor fuel into the intake air system can be modified as follows. That is, the vapor fuel absorbed by the canister from the fuel tank may be suctioned into and pressurized within a pressurizing pump. Then, the pressurized vapor fuel may be discharged into a pressure tank maintained at a high pressure to liquefy the vapor fuel. Thereafter, the liquefied fuel under the high pressure may be discharged into a fuel supply line.




However, when the pump suctions the vapor fuel from the canister, the air is also suctioned along with the vapor fuel, so that the air is also dissolved into the pressurized liquefied fuel. Thus, the fuel that contains the dissolved air is supplied to the engine. When the fuel pressure decreases, for example, right after engine stop, the air dissolved in the fuel is depressurized and becomes air bubbles, making it difficult to restart the engine.




SUMMARY OF THE INVENTION




Thus, it is an objective of the present invention to provide a vapor fuel processing system that can process vapor fuel regardless of a degree of a negative pressure of intake air and can restrain a deviation in an air-fuel ratio.




To achieve the objective of the present invention, there is provided a vapor fuel processing system including a fuel tank, a pressure tank, a pressure control valve, a canister and a pressurizing pump. The fuel tank receives liquid fuel. The pressure tank is arranged within the fuel tank and receives liquid fuel supplied from the fuel tank. The pressure control valve is arranged between the fuel tank and the pressure tank. The pressure control valve is opened to communicate between an inside of the pressure tank and an inside of the fuel tank when a pressure within the pressure tank becomes equal to or greater than a predetermined pressure. The canister absorbs vapor fuel contained in the fuel tank. The pressurizing pump is arranged between the canister and the pressure tank. The pressurizing pump suctions the vapor fuel from the canister and discharges the vapor fuel into the liquid fuel in the pressure tank upon pressurizing the vapor fuel in the pressurizing pump to dissolve the vapor fuel into the liquid fuel in the pressure tank.











BRIEF DESCRIPTION OF THE DRAWINGS




The invention, together with additional objectives, features and advantages thereof, will be best understood from the following description, the appended claims and the accompanying drawings in which:





FIG. 1

is a schematic view of a vapor fuel processing system according to a first embodiment of the present invention;





FIG. 2

is a schematic view of a vapor fuel processing system according to a second embodiment of the present invention; and





FIG. 3

is a schematic view of a vapor fuel processing system according to a third embodiment of the present invention.











DETAILED DESCRIPTION OF THE INVENTION




Various embodiments of the present invention will be described with reference to the accompanying drawings.




First Embodiment




A vapor fuel processing system according to a first embodiment of the present invention is shown in FIG.


1


.




There is provided a fuel tank


1


that can be made of a resin material or a metal material. A pressure control valve


50


is provided within the fuel tank


1


. When a pressure in the fuel tank


1


becomes negative, the pressure control valve


50


is opened to connect an inside and an outside of the fuel tank


1


.




The fuel pump


10


is an in-tank type fuel pump that is received within the fuel tank


1


. The fuel pump


10


includes a flange


11


, a pump main body


12


, suction filters


13


,


14


and a pressure regulator


15


. The flange


11


is attached to the fuel tank


1


. Various fuel pipelines, connectors and the like are attached to the flange


11


. Furthermore, a pressurizing pump


40


, which will be described later in greater detail, is integrally mounted to the flange


11


. Thus, the fuel pump


10


and the pressurizing pump


40


constituting an integrated unit that may be preassembled before it is installed in the fuel tank


1


. The integrated unit allows easier assembly of the vapor fuel processing system and also allows a reduction in the number of the assembling steps for assembling the vapor fuel processing system.




The pump main body


12


is of a two-stage type. In a first stage, the pump main body


12


suctions fuel from the fuel tank


1


through the suction filter


13


and discharges it into a pressure tank


20


. Then, in a second stage, the pump main body


12


suctions the fuel from the pressure tank


20


through the suction filter


14


and pressurizes it. Then, the pump main body


12


discharges the pressurized fuel toward an engine side of the system through a fuel discharge pipeline


100


. A pressure regulator


15


regulates a pressure of the pressurized fuel discharged from the pump main body


12


to be equal to or less than a predetermined value. The pressure regulator


15


also returns excess fuel into the pressure tank


20


. The pressure tank


20


is substantially sealed. A pressure control valve


52


is opened to communicate between the inside of the fuel tank


1


and an inside of the pressure tank


20


when a pressure in the pressure tank


20


becomes equal to or greater than a predetermined pressure.




A canister


30


is arranged at the outside of the fuel tank


1


and receives activated carbons for absorbing vapor fuel outputted from the fuel tank


1


. The canister


30


has a heater


31


and a solenoid valve


32


. The heater


31


that acts as a heating means of the present invention heats an inside of the canister


30


to increase the amount of fuel removed from the activated carbons of the canister


30


. When the solenoid valve


32


is opened, the inside and an outside of the canister


30


are communicated with each other, so that the inside of the canister


30


is communicated with the atmosphere. A pipeline


110


connects between a pressure control valve


51


provided in the fuel tank


1


and the canister


30


. The pressure control valve


51


opens to communicate between the inside of the fuel tank


1


and the inside of the canister


30


when the pressure in the fuel tank


1


becomes equal to or greater than a predetermined pressure. A pipeline


111


connects between the canister


30


and the pressurizing pump


40


. A pipeline


112


connects between the pressurizing pump


40


and the pressure tank


20


. The pipelines


110


,


111


,


112


constitute a circulation pipeline for circulating air received in the fuel tank


1


between the fuel tank


1


and the canister


30


.




The pressurizing pump


40


is assembled to the flange


11


. The pressurizing pump


40


is driven, for example, by a motor to suction the vapor fuel received in the canister


30


and to pressurize it to a pressure equal to or less than 100 kPa. The pressurized vapor fuel is then discharged from the pressurizing pump


40


into the pressure tank


20


.




In general, in order to liquefy the vapor fuel, the vapor fuel should be cooled to about zero degrees Celsius or should be pressurized to about 500 to 600 kPa. In the present embodiment, the vapor fuel is absorbed by the canister


30


when it is supplied from the fuel tank


1


through the pipeline


110


, and then the vapor fuel is suctioned from the canister


30


by the pressurizing pump


40


through the pipeline


111


. Thereafter, the vapor fuel is pressurized by the pressurizing pump


40


and is discharged into the pressure tank


20


through the pipeline


112


, so that the vapor fuel is dissolved into the liquid fuel received in the pressure tank


20


. The vapor fuel dissolved into the liquid fuel received in the pressure tank


20


is suctioned by the pump main body


12


and is thereafter discharged from the pump main body


12


toward the engine side of the system. The air discharged into the pressure tank


20


along with the vapor fuel is discharged into the fuel tank


1


through the pressure control valve


52


and flows into the canister


30


along with the remaining air and the vapor fuel in the fuel tank


1


once again.




When the vapor fuel is pressurized to about equal to or less than 100 kPa without cooling it, the most of the vapor fuel can be dissolved into the liquid fuel in the pressure tank


20


without cooling it. This allows use of a smaller pressurizing pump having a smaller pressurizing capacity as the pressurizing pump


40


of the present embodiment. Furthermore, it is also possible to prevent leakage of the vapor fuel out of the fuel tank


1


.




In the present embodiment, the temperature in the canister


30


is raised by the heater


31


. The removal process of the vapor fuel absorbed by the activated carbons in the canister


30


is an endothermic reaction. Thus, when the temperature of the canister


30


increases, the amount of the vapor fuel removed from the canister


30


increases, so that a concentration of the vapor fuel discharged into the pressure tank


20


increases. When the concentration of the vapor fuel discharged into the pressure tank


20


increases, the vapor fuel is more easily dissolved into the liquid fuel received within the pressure tank


20


.




When the temperature inside of the fuel tank


1


rises, a concentration of the vapor fuel supplied to the canister


30


tends to increase. Thus, it is advantageous to provide, for example, a cooling device at an inlet side of the pressure control valve


51


to reduce a temperature of the air in order to reduce the concentration of the vapor fuel supplied to the canister


30


.




Also, when the amount of the vapor fuel removed from the canister


30


increases, the amount of the vapor fuel that can be absorbed by the canister


30


increases. Thus, a size of the canister according to the present embodiment can be advantageously reduced in comparison to a canister that is not heated while a capacity of the canister for absorbing the vapor fuel is maintained at substantially the same level.




Second Embodiment




A second embodiment of the present invention is shown in FIG.


2


. Components similar to those of the first embodiment are depicted with similar reference numerals. In the second embodiment, in addition to the passage for discharging the vapor fuel from the canister


30


into the pressure tank


20


, there is also provided a passage for discharging the vapor fuel from the canister


30


into an intake air pipeline that constitutes a part of an intake air system.




A pipeline (output pipeline)


120


branches off from the pipeline


111


and is connected to the intake air pipeline (not shown). A check valve


60


is inserted in the pipeline


120


on the canister


30


side. The check valve


60


prevents backflow of the vapor fuel from the intake air pipeline side toward the canister


30


side thereof. A solenoid valve


61


is inserted in the pipeline


120


on the intake air pipeline side of the check valve


60


. When the solenoid valve


61


is opened, the canister


30


side is communicated with the intake air pipeline side, so that the vapor fuel within the canister


30


is discharged to the intake air pipeline side. The pipeline


120


and the solenoid valve


61


constitute an outputting means of the present invention.




When an ambient temperature rises, and thereby a large amount of the vapor fuel is generated in the fuel tank


1


, it could happen that the pressurizing pump


40


alone is not sufficient to process the vapor fuel within the canister


30


by discharging the vapor fuel into the pressure tank


20


. When a pressure sensor (not shown) senses that the pressure inside of the fuel tank


1


becomes equal to or greater than a predetermined pressure, the solenoid valve


61


is opened, so that the vapor fuel that has not been discharged into the pressure tank


20


by the pressurizing pump


40


is discharged to the intake air pipeline side.




The amount of the vapor fuel discharged into the intake air pipeline side should be small, so that a deviation in an air-fuel ratio is small. Furthermore, by opening the solenoid valve


61


, the vapor fuel is processed through the two systems, so that the amount of the vapor fuel removed from the canister


30


is increased, and thereby the amount of the vapor fuel that can be absorbed by the canister


30


is increased. Thus, a size of the canister can be further reduced in comparison to the canister of the first embodiment while the amount of the vapor fuel that can be absorbed by the canister remains substantially the same. Furthermore, depending on the amount of the vapor fuel generated in the fuel tank


1


, it is possible to eliminate the heater


31


.




Third Embodiment




A third embodiment of the present invention is shown in FIG.


3


. Components similar to those of the first embodiment are depicted with similar reference numerals. In the third embodiment, a subtank


70


and a pressure tank


75


are provided as separate components. The pump main body


12


suctions the fuel from the subtank


70


, and the vapor fuel pressurized by the pressurizing pump


40


is discharged into the pressure tank


75


.




A known jet pump (not shown) is connected to a distal end of a pipeline


130


for circulating the excess fuel from the pressure regulator


15


. A fuel level in the subtank


70


is maintained to be higher than a fuel level in the fuel tank


1


by the fuel injected through the jet pump.




The fuel circulated from the pressure regulator


15


is also circulated to the pressure tank


75


through a pipeline


131


. A choke


132


is provided in the pipeline


131


. By adjusting an opening area of the choke


132


, a ratio between the amount of the fuel to be circulated to the jet pump and the amount of the fuel to be circulated to the pressure tank


75


can be adjusted. The fuel circulated to the pipeline


131


flows into the pressure tank


75


from the choke


132


through a check valve


76


. The check valve


76


prevents backflow of the fuel from the pressure tank


75


to the pressure regulator


15


side, so that the check valve


76


maintains a pressure in the pressure tank


75


when the engine is stopped.




As described above, in each one of the above embodiments, the vapor fuel is dissolved into the liquid fuel in the pressure tank. Thus, substantially no vapor fuel is discharged to the engine side, or only a small amount of the vapor fuel is discharged to the engine side, if any. Thus, even if the air-fuel ratio is deviated, the amount of the deviation in the air-fuel ratio can be minimized, so that noxious components contained in exhaust gas of the vehicle can be accordingly reduced.




Furthermore, the vapor fuel can be processed regardless of a degree of a negative pressure of the intake air, so that fuel consumption can be improved. Thus, if the vapor fuel processing system of the present invention is implemented in a low emission engine that has a smaller pumping loss and a wider lean fuel range, the vapor fuel can be effectively processed, so that the amount of the noxious components contained in the exhaust gas can be relatively easily reduced.




In the above embodiments of the present invention, although the fuel pump is received within the fuel tank


1


, it is possible to arrange the fuel pump at the outside of the fuel tank


1


. Furthermore, the pressurizing pump and the pressure tank can be also arranged at the outside of the fuel tank


1


.




Additional advantages and modifications will readily occur to those skilled in the art. The invention in its broader terms is therefore, not limited to the specific details, representative apparatus, and illustrative examples shown and described.



Claims
  • 1. A vapor fuel processing system comprising:a fuel tank for receiving liquid fuel; a pressure tank arranged within said fuel tank, said pressure tank receiving liquid fuel supplied from said fuel tank; a pressure control valve arranged between said fuel tank and said pressure tank, said pressure control valve being opened to communicate between an inside of said pressure tank and an inside of said fuel tank when a pressure within said pressure tank becomes equal to or greater than a predetermined pressure; a canister for absorbing vapor fuel contained in said fuel tank; and a pressurizing pump arranged between said canister and said pressure tank, said pressurizing pump suctioning said vapor fuel from said canister and discharging said vapor fuel into said liquid fuel in said pressure tank upon pressurizing said vapor fuel in said pressurizing pump to dissolve said vapor fuel into said liquid fuel in said pressure tank.
  • 2. A vapor fuel processing system according to claim 1, further comprising a heating means arranged within said canister for heating an inside of said canister.
  • 3. A vapor fuel processing system according to claim 1, further comprising an outputting means for outputting said vapor fuel absorbed within said canister to an intake air system.
  • 4. A vapor fuel processing system according to claim 1, further comprising a fuel pump received within said fuel tank, said fuel pump pumping said liquid fuel received within said fuel tank toward an engine side of said vapor fuel processing system.
  • 5. A vapor fuel processing system according to claim 4, wherein said pressurizing pump and said fuel pump are provided together as an integrated unit.
  • 6. A vapor fuel processing system according to claim 1, wherein said canister is inserted in a circulation pipeline that circulates air received within said fuel tank between said fuel tank and said canister, said vapor fuel absorbed by said canister being removed from said canister with use of said air circulated through said circulation pipeline.
  • 7. A vapor fuel processing system according to claim 3, wherein said outputting means including:an output pipeline arranged between said canister and said intake air system to communicate therebtween; and a solenoid valve inserted in said output pipeline, said solenoid valve being opened when a pressure in said fuel tank becomes equal to or greater than a predetermined pressure.
  • 8. A vapor fuel processing system according to claim 4, wherein said fuel pump includes a pump main body received within said pressure tank.
  • 9. A vapor fuel processing system according to claim 4, wherein said fuel pump includes a pump main body arranged at an outside of said pressure tank.
Priority Claims (1)
Number Date Country Kind
2000-320835 Oct 2000 JP
US Referenced Citations (5)
Number Name Date Kind
4059081 Kayanuma Nov 1977 A
4829968 Onufer May 1989 A
5275145 Tuckey Jan 1994 A
5931141 Chino Aug 1999 A
6014958 Miwa et al. Jan 2000 A
Foreign Referenced Citations (1)
Number Date Country
58-136660 Sep 1983 JP