Method for removing residual purge gas
11168626 ยท 2021-11-09
Assignee
Inventors
Cpc classification
F02M25/0872
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F02D41/18
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F02D41/042
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F02D41/0047
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F02M25/0854
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F02D41/0032
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F02M26/47
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F02M35/10373
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F02D41/0072
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F02M25/0836
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
International classification
F02D41/00
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F02M25/08
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F02M26/47
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
Abstract
The present disclosure relates to a method for removing residual purge gas in operating an active purge system and includes determining evaporation gas purge stop in a control unit, closing a PCSV mounted on a purge line connecting a canister and an intake pipe, and determining whether all of the evaporation gas flowed into the intake pipe is flowed into a combustion chamber, so that all of the evaporation gas flowed into an intake pipe during travelling can be flowed into and combusted in the combustion chamber.
Claims
1. A method for removing residual purge gas in operating an active purge system, the method comprising: determining an evaporation gas purge stop; closing a PCSV (pressure control solenoid valve) mounted on a purge line connecting a canister and an intake pipe; determining whether all evaporation gas flowed into the intake pipe through the PCSV has flowed into a combustion chamber when an amount of an air supplied to the combustion chamber after the PCSV is closed is equal to or greater than a first predetermined value or when a time elapsed after the PCSV is closed exceeds a second predetermined value; and stopping an engine when it is determined that all evaporation gas has flowed into the combustion chamber.
2. The method of claim 1, wherein the PCSV is ready to operate again after a predetermined critical time has elapsed after it is determined that all of the evaporation gas has flowed into the combustion chamber.
3. The method of claim 1, wherein an active purge pump is mounted on the purge line so as to be located between the PCSV and the canister, the method further comprising adjusting a rotation speed of the active purge pump, an opening amount of the PCSV and an opening and closing timing of the PCSV.
4. The method of claim 3, wherein the adjusting is based on signals received from a sensor mounted on the canister, a sensor mounted on the intake pipe, a sensor mounted on an exhaust pipe connected with the combustion chamber, and a plurality of sensors mounted on the purge line.
5. A method for removing residual purge gas in operating an active purge system, the method comprising: determining an evaporation gas purge stop; closing a PCSV (pressure control solenoid valve) mounted on a purge line connecting a canister and an intake pipe; determining whether all evaporation gas flowed into the intake pipe through the PCSV has flowed into a combustion chamber when an amount of an air supplied to the combustion chamber after the PCSV is closed is equal to or greater than a first predetermined value or when a time elapsed after the PCSV is closed exceeds a second predetermined value, wherein determining whether all of the evaporation gas has flowed into the combustion chamber is based on an evaporation gas remaining signal; and stopping an engine when it is determined that all evaporation gas has flowed into the combustion chamber.
6. The method of claim 5, wherein the evaporation gas remaining signal is derived by comparing whether an amount of an air supplied to the combustion chamber after the PCSV has closed, is equal to or greater than the first predetermined value.
7. The method of claim 6, wherein the evaporation gas remaining signal is derived by comparing a value obtained by subtracting an (exhaust gas recirculation) EGR gas amount from the amount of air with an effective intake system volume.
8. The method of claim 5, wherein the evaporation gas remaining signal is derived based on a delay time derived from a delay model function modeling the flow until the evaporation gas has flowed from the intake pipe to an intake manifold and a density of the evaporation gas.
9. The method of claim 5, wherein the evaporation gas remaining signal is derived based on a delay time derived from a delay model function modeling the flow until the evaporation gas has flowed from the intake pipe to an intake manifold and concentration factors of the evaporation gas.
10. A method for removing residual purge gas in operating an active purge system, the method comprising: determining an evaporation gas purge stop; closing a PCSV (pressure control solenoid valve) mounted on a purge line connecting a canister and an intake pipe; determining whether all evaporation gas flowed into the intake pipe through the PCSV has flowed into a combustion chamber when an amount of an air supplied to the combustion chamber after the PCSV is closed is equal to or greater than a first predetermined value or when a time elapsed after the PCSV is closed exceeds a second predetermined value, the determining being based on an evaporation gas remaining signal; and stopping an engine when it is determined that all evaporation gas has flowed into the combustion chamber, wherein the PCSV is ready to operate again after a predetermined critical time has elapsed after it is determined that all of the evaporation gas has flowed into the combustion chamber.
11. The method of claim 10, wherein an active purge pump is mounted on the purge line so as to be located between the PCSV and the canister, the method further comprising adjusting a rotation speed of the active purge pump, an opening amount of the PCSV and an opening and closing timing of the PCSV.
12. The method of claim 11, wherein the adjusting is based on signals received from a sensor mounted on the canister, a sensor mounted on the intake pipe, a sensor mounted on an exhaust pipe connected with the combustion chamber, and a plurality of sensors mounted on the purge line.
13. The method of claim 10, wherein the evaporation gas remaining signal is derived by comparing whether an amount of an air supplied to the combustion chamber after the PCSV has closed, is equal to or greater than the first predetermined value.
14. The method of claim 13, wherein the evaporation gas remaining signal is derived by comparing a value obtained by subtracting an (exhaust gas recirculation) EGR gas amount from the amount of air with an effective intake system volume.
15. The method of claim 10, wherein the evaporation gas remaining signal is derived based on a delay time derived from a delay model function modeling the flow until the evaporation gas has flowed from the intake pipe to an intake manifold and a density of the evaporation gas.
16. The method of claim 10, wherein the evaporation gas remaining signal is derived based on a delay time derived from a delay model function modeling the flow until the evaporation gas has flowed from the intake pipe to an intake manifold and concentration factors of the evaporation gas.
17. The method of claim 5, wherein an active purge pump is mounted on the purge line so as to be located between the PCSV and the canister, the method further comprising adjusting a rotation speed of the active purge pump, an opening amount of the PCSV and an opening and closing timing of the PCSV.
18. The method of claim 17, wherein the adjusting is based on signals received from a sensor mounted on the canister, a sensor mounted on the intake pipe, a sensor mounted on an exhaust pipe connected with the combustion chamber, and a plurality of sensors mounted on the purge line.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
(1) The above and other objects, features and advantages of the present disclosure will be more clearly understood from the following detailed description taken in conjunction with the accompanying drawings, in which:
(2)
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DETAILED DESCRIPTION OF ILLUSTRATIVE EMBODIMENTS
(5) Hereinafter, a flowchart of a method for removing residual purge gas in operating an active purge system according to an exemplary embodiment of the present disclosure will be described in detail with reference to accompanying drawings.
(6) As shown in
(7) The control unit may include a hybrid control unit for controlling the operation of a hybrid vehicle and an engine control unit for controlling the operation of an engine. The control unit may include an evaporation gas purge execution program and an evaporation gas purge stop program. The control unit may perform the evaporation gas purge stop program and the evaporation gas purge execution program based on signals received from various sensors.
(8) The evaporation gas purge execution program may be performed based on signals received from a plurality of sensors mounted on a pedal, the canister 100, the purge line 200, the intake pipe I and an exhaust pipe E. The evaporation gas purge execution program, as shown in
(9) The evaporation gas is compressed in the purge line between the active purge pump 300 and the PCSV 400 through adjustment of the rotation speed of the active purge pump 300 and opening and closing timing control of the PCSV 400 and opening amount adjustment of the PCSV 400, and then can be forcibly injected into the intake pipe I. Thus, evaporator gas can be injected into the intake pipe I even though the intake pipe I is equipped with a supercharger and the internal pressure of the intake pipe I is equal to or higher than the atmospheric pressure. Particularly, through the pressure generated by compressing the evaporation gas between the active purge pump 300 and the PCSV 400 among the purge line and the opening and closing timing and opening control of the PCSV 400, it is possible to the amount of the evaporation gas flowing into the intake pipe I from the purge line 200. The rotation speed control of the active purge pump 300 can produce a pressure difference between the front and rear ends of the active purge pump 300. The hydrocarbon concentration of the evaporation gas concentrated between the active purge pump 300 and the PCSV 400 by the pressure difference can be calculated. The hydrocarbon density can be calculated from the hydrocarbon concentration and the fuel amount supplied to the combustion chamber can be controlled based on the hydrocarbon density.
(10) The evaporation gas purge execution program may estimate the purge flow rate, which is the amount of evaporation gas to be removed from the canister 100, based on the signal received from the sensor mounted on the canister 100. The evaporation gas purge execution program may calculate a target purge flow rate based on the intake amount, fuel injection amount, and purge flow rate in the current running state. The target purge flow rate is the amount that should be flowed from the purge line 200 into the intake pipe I to satisfy the purge flow rate. In addition to calculate the target purge flow rate, the pressure between the active purge pump 300 and the PCSV 400 in the purge line to meet the target purge flow rate, the rotation speed of the active purge pump 300, the opening and closing timing of the PCSV 400, and the opening amount of the PCSV 400 may be derived. Additionally, as the target purge flow rate is forcibly flowed into the intake pipe I, the correction value of the fuel injection amount being injected into the combustion chamber R may be also derived, considering that hydrocarbon is additionally supplied to the combustion chamber R.
(11) The evaporation gas purge stop program may be executed at the moment of determining the engine stop for the driving control or operation control in the control unit. The step S100 of determining whether the evaporation gas purge stops or not may be performed at the same time of executing the evaporation gas purge stop program. The evaporation gas purge stop program may stop the evaporation gas purge execution program. When it is determined that all of the evaporation gas combustion is flowed into combustion chamber R in the step S300 of determining whether all the evaporation gas flowed into the intake pipe I is flowed into the combustion chamber R, the evaporation gas purge stop program is stopped. The engine may be stopped together with the stop of the evaporation gas purge stop program. After the evaporation gas purge stop program is stopped, the evaporation gas purge execution program is activated after the critical time is elapsed.
(12) Even if the engine stop is determined, since the engine is stopped after it is determined that all of the evaporation gas is flowed into the combustion chamber R, purge missing of the evaporation gas flowed into the intake pipe I due to the engine stop may be prevented. Since the purge missing of the evaporation gas is prevented, the evaporation gas may be prevented from leaking into the atmosphere.
(13) In the step S200 of closing the PCSV 400, it may be repeatedly checked whether the amount of evaporation gas collected in the canister 100 is equal to or less than an appropriate value. When it is confirmed that the amount of evaporation gas collected in the canister 100 is equal to or less than an appropriate value, the PCSV 400 may be closed. In the step S200 of closing the PCSV 400, the control unit may check whether the purge flow rate is deviated from the canister 100 based on the signal received from the sensor mounted on the canister 100. Together with this, it may be confirmed that the target purge flow rate is forcibly injected from the purge line 200 to the intake pipe I based on signals continuously received from the first pressure sensor 500 and second pressure sensor 600 mounted on the purge line 200. The control unit may close the PCSV 400 when it is confirmed that both the purge flow rate and the target purge flow rate are satisfied.
(14) In the step S300 of determining whether all of the evaporation gas is flowed into the combustion chamber R, it may be determined whether all of the evaporation gas is flowed into the combustion chamber R based on the evaporation gas remaining signal. The evaporation gas remaining signal, as shown in
(15) The evaporation gas remaining signal is changed from ON to OFF when the integrated value of the amount of air supplied to the combustion chamber R after the closing of the PCSV 400 is above the predetermined value or when the elapsed time after the closing of the PCSV 400 exceeds the predetermined value.
(16) According to the exemplary embodiment, the evaporation gas remaining signal may be derived by comparing the value obtained by subtracting the EGR gas amount from the integrated value of the air amount and the effective intake system volume, which is the intake volume actually flowed into the combustion chamber R by RPM or LOAD. When the effective intake system volume is greater than the value obtained by subtracting the EGR gas amount from the integrated value of the air amount, the evaporation gas remaining signal is changed from ON to OFF.
(17) According to another exemplary embodiment, the evaporation gas remaining signal may be derived based on the delay time derived from the delay model function modeling the flow until the evaporation gas is flowed from the intake pipe I into the intake manifold, and the density or concentration factors of the evaporation gas.
(18) The evaporation gas remaining signal may be changed from ON to OFF when the value calculated by substituting the delay time and density into a specific formula is greater than or less than the predetermined value. Alternatively, the evaporation gas remaining signal may be changed from ON to OFF when the difference value between the delay time and density, and the value calculated by multiplying the delay time and the density is greater than or less than the predetermined value.
(19) According to the method for removing residual purge gas in operating an active purge system of an exemplary embodiment of the present disclosure as configured above, all of the evaporation gas flowed into the intake pipe I during operation can be flowed into and combusted in the combustion chamber R.
(20) Particularly, since it is determined whether all of the evaporation gas flowed into the intake pipe I after the PCSV 400 is closed is flowed into the combustion chamber R, the stopping point of the engine due to the control during the vehicle operation can be delayed after all of the evaporation gas is flowed into the combustion chamber R.
(21) Therefore, Even if the engine is stopped due to the control during operation, the purge treatment of the evaporation gas flowed into to the intake pipe I is prevented from being missed. Evaporation gas that is missing the purge treatment is prevented from leaking into the atmosphere.
(22) In accordance with the method for removing residual purge gas in operating the active purge system of an exemplary embodiment of the present disclosure as configured above, all of the evaporation gas flowed into the intake pipe during operation can be flowed into and combusted in the combustion chamber.
(23) Particularly, since it is determined that all the evaporation gas flowed into the intake pipe is flowed into the combustion chamber after the PCSV is closed, the stopping point of the engine due to the control during the vehicle operation can be delayed after all of the evaporation gas is flowed into the combustion chamber.
(24) Therefore, even if the engine is stopped due to control during operation, the purging treatment of the evaporation gas flowed into the intake pipe is prevented from being omitted. Evaporation gas that is missing the purge treatment is prevented from leaking into the atmosphere.