FUEL-CELL HYDROGEN RECYCLING MEANS

Abstract

A fuel-cell hydrogen recycling system, comprising a fuel cell; a controller; a hydrogen recycling pipeline provided with a hydrogen circulating pump and a check valve; an air inlet pipeline and an air outlet pipeline connected to the fuel cell, respectively; a hydrogen inlet pipeline provided with a hydrogen inlet valve; and a hydrogen outlet pipeline provided with a hydrogen outlet valve, with the hydrogen recycling pipeline connected to the hydrogen inlet pipeline, wherein the system further comprises a gas-liquid separating reservoir, which comprises a reservoir positioned at its upper portion and a gas-liquid separator positioned at its lower portion communicated with each other vertically, the reservoir is connected to the hydrogen outlet pipeline and the hydrogen recycling pipeline, respectively, and the gas-liquid separator discharges exhaust water and redundant nitrogen through a exhaust pipeline that is provided with a ventilation valve.

Claims

1.-10. (canceled)

11. A fuel cell hydrogen recycling system, at least comprising a fuel cell, a controller and a gas-liquid separating reservoir comprising a reservoir positioned at its upper portion and a gas-liquid separator positioned at its lower portion which are connected to each other vertically, wherein the reservoir is connected to a hydrogen exhaust pipeline and a hydrogen recycling pipeline respectively, the hydrogen exhaust pipeline of the fuel cell is provide with a hydrogen outlet valve, the hydrogen recycling pipeline is provided with a hydrogen circulating pump and a check valve, a period between adjacent venting states is defined as a venting cycle of electrochemical reaction of a stack, during the same venting cycle of electrochemical reaction of a stack, the hydrogen outlet valve opens for one or more times with a constant interval therebetween, the hydrogen circulating pump and the check valve open for only one time.

12. The fuel cell hydrogen recycling system of claim 11, wherein during the same venting cycle of electrochemical reaction of a stack, an opening frequency of the hydrogen outlet valve is 1-10 times of an opening frequency of the hydrogen circulating pump.

13. The fuel cell hydrogen recycling system of claim 11, wherein a pressure sensor connected to the controller is provided between the hydrogen outlet valve and an inlet of the reservoir, during the same venting cycle of electrochemical reaction of a stack, opening the hydrogen outlet valve to enter the system into its venting state, and after exhaust gas containing water, nitrogen and hydrogen enters the reservoir and when the pressure of the exhaust gas as detected by the pressure sensor is higher than a preset pressure upper limit, opening both the hydrogen circulating pump and the check valve to draw the hydrogen in the reservoir back to the hydrogen inlet pipeline.

14. The fuel cell hydrogen recycling system of claim 12, wherein the gas-liquid separator discharges exhaust water and redundant nitrogen through an exhaust pipeline that is provided with a ventilation valve, inside the reservoir there is a nitrogen concentration meter connected to the controller, inside the gas-liquid separator there is a level gauge connected to the controller, the gas-liquid separator is connected to the ventilation valve, when the concentration of nitrogen in the reservoir as measured by the nitrogen concentration meter is higher than a preset nitrogen concentration threshold or when a water level as measured by the level gauge is higher than a present water level threshold, the controller opens the ventilation valve to discharge the separated liquid water and redundant nitrogen and closes the ventilation valve until clearance.

15. The fuel cell hydrogen recycling system of claim 14, wherein the gas-liquid separator is installed in the lower part of the reservoir, so that nitrogen and liquid water that have relatively high specific gravities can be discharged smoothly and effectively.

16. A fuel cell system, at least comprising a fuel cell and a controller, wherein the system further comprises a gas-liquid separating reservoir comprising a reservoir positioned at its upper portion and a gas-liquid separator positioned at its lower portion structured with each other connected vertically, the reservoir is connected to a hydrogen exhaust pipeline and a hydrogen recycling pipeline, respectively, and the gas-liquid separator discharges exhaust water and redundant nitrogen through an exhaust pipeline that is provided with a ventilation valve, inside the gas-liquid separator there is a level gauge connected to the controller, when a water level as measured by the level gauge is higher than a present water level threshold, the controller opens the ventilation valve to discharge the separated liquid water and redundant nitrogen, so that the controller controls the opening and closing of the ventilation valve according to liquid water level, wherein a period between adjacent venting states is defined as a venting cycle of electrochemical reaction of a stack, during the same venting cycle of electrochemical reaction of a stack, the hydrogen outlet valve opens for one or more times with a constant interval therebetween, the hydrogen circulating pump does not need to open or close following the hydrogen outlet valve every time during the same venting cycle of electrochemical reaction of a stack, an opening frequency of the hydrogen outlet valve is 1-10 times of an opening frequency of the hydrogen circulating pump.

17. The fuel cell system of claim 16, wherein a period between adjacent venting states is defined as a venting cycle of electrochemical reaction of a stack, during the same venting cycle of electrochemical reaction of a stack, the hydrogen circulating pump and the check valve open for only one time.

18. The fuel cell system of claim 16, wherein a pressure sensor connected to the controller is provided between the hydrogen outlet valve and an inlet of the reservoir, during the same venting cycle of electrochemical reaction of a stack, opening the hydrogen outlet valve to enter the system into its venting state, and after exhaust gas containing water, nitrogen and hydrogen enters the reservoir and when the pressure of the exhaust gas as detected by the pressure sensor is higher than a preset pressure upper limit, opening both the hydrogen circulating pump and the check valve to draw the hydrogen in the reservoir back to the hydrogen inlet pipeline.

19. The fuel cell system of claim 16, wherein at least one cooling fin is arranged along the hydrogen outlet pipeline, in the section from the hydrogen outlet valve to the inlet of the reservoir, on the outer wall of the gas-liquid separating reservoir or on the inner wall of the reservoir, the cooling fin improves efficiency of gas-liquid separation by cooling high-temperature exhaust gas to ambient temperature.

20. The fuel cell system of claim 19, wherein the exhaust pipeline converges to an air exhaust pipeline, and the compound pipeline after converging is provided with a gas mixer to evenly mix the hydrogen intermittently discharged by the exhaust pipeline and air so as to reduce a concentration of hydrogen.

21. A method of recycling hydrogen for a fuel cell, wherein the method at least comprises: i) opening a hydrogen inlet valve and keeping a hydrogen inlet pipeline unobstructed, while keeping a hydrogen outlet valve, a check valve, a hydrogen circulating pump and a ventilation valve closed, for starting up reaction of stack of the fuel cell; ii) during a venting cycle of electrochemical reaction of the stack, opening the hydrogen outlet valve to set the fuel cell into a venting state, and after exhaust gas containing water, nitrogen and hydrogen entering a reservoir and once a pressure of the exhaust gas detected by a pressure sensor going higher than a preset pressure upper limit, both the hydrogen circulating pump and the check valve are opened at the same time to draw the hydrogen in the reservoir back to the hydrogen inlet pipeline; wherein a period between adjacent venting states is defined as a venting cycle of electrochemical reaction of a stack, during the same venting cycle of electrochemical reaction of a stack, the hydrogen outlet valve opens for one or more times with a constant interval therebetween, the hydrogen circulating pump and the check valve open for only one time.

22. The method of recycling hydrogen for a fuel cell of claim 21, wherein the method further comprises: when the concentration of nitrogen in the reservoir as measured by a nitrogen concentration meter is higher than a preset nitrogen concentration threshold or when a water level as measured by a level gauge is higher than a present water level threshold, opening the ventilation valve to discharge the separated liquid water and redundant nitrogen and closes the ventilation valve until clearance; when the pressure of exhaust gas as detected by the pressure sensor is lower than a preset pressure lower limit, closing the hydrogen circulating pump and the stop valve, and starting control of the next venting cycle of the electrochemical reaction of the stack.

23. The method of recycling hydrogen for a fuel cell of claim 21, wherein the method further comprises: the hydrogen circulating pump does not have to open and close along with the hydrogen outlet valve every time, an opening frequency of the hydrogen outlet valve is 1-10 times of an opening frequency of the hydrogen circulating pump.

24. The method of recycling hydrogen for a fuel cell of claim 21, wherein the method further comprises: arranging a gas mixer on a compound connected pipeline formed by the exhaust pipeline converging to an air exhaust pipeline to evenly mix the hydrogen intermittently discharged by the exhaust pipeline and air so as to reduce a concentration of hydrogen.

25. The method of recycling hydrogen for a fuel cell of claim 24, wherein the method further comprises: arranging at least one cooling fin along the hydrogen outlet pipeline, in the section from the hydrogen outlet valve to the inlet of the reservoir, on the outer wall of the gas-liquid separating reservoir or on the inner wall of the reservoir, the cooling fin improving efficiency of gas-liquid separation by cooling high-temperature exhaust gas to ambient temperature.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

[0024] FIG. 1 is a schematic structural drawing of a means of the present invention;

[0025] FIG. 2 is a control sequence diagram of the present invention.

DETAILED DESCRIPTION OF THE INVENTION

[0026] The invention as well as a preferred mode of use, further objectives and advantages thereof will be best understood by reference to the following detailed description of illustrative embodiments when read in conjunction with the accompanying drawings.

Embodiment

[0027] As shown in FIG. 1, the present invention provides a fuel-cell hydrogen recycling means, which comprises a fuel cell 1; a controller; a hydrogen recycling pipeline provided with a hydrogen circulating pump 4 and a check valve 5; an air inlet pipeline 11 and an air outlet pipeline 10 connected to the fuel cell 1, respectively; a hydrogen inlet pipeline 8 provided with a hydrogen inlet valve 2; and a hydrogen outlet pipeline 9 provided with a hydrogen outlet valve 3. The hydrogen recycling pipeline is connected to the hydrogen inlet pipeline 8. The means further comprises an integrated gas-liquid separating reservoir 6. The gas-liquid separating reservoir 6 comprises a reservoir 61 arranged at an upper portion and a gas-liquid separator 62 arranged at a lower portion, which are integrated as a unity or separated but communicated with each other through mesh. The reservoir 61 is connected to the hydrogen outlet pipeline 9 and the hydrogen recycling pipeline, respectively. The gas-liquid separator 62 discharges exhaust water and redundant nitrogen through an exhaust pipeline that is provided with a ventilation valve 7. The controller is connected to the hydrogen circulating pump 4, the check valve 5, the ventilation valve 7, the hydrogen outlet valve 3, and the hydrogen inlet valve 2, respectively. The reservoir 61 has a pressure sensor 611, which is connected to the controller, arranged at its joint with the hydrogen exhaust pipeline 9.

[0028] Inside the reservoir 61 there is a nitrogen concentration meter 612 connected to the controller for detecting the concentration of nitrogen.

[0029] Inside the gas-liquid separator 62 there is a level gauge 621 connected to the controller for detecting the level of liquid water.

[0030] The exhaust pipeline converges to the air exhaust pipeline 10, and the compound pipeline after converging is provided with a gas mixer 14 for even mixing and turbulence forming. The gas mixer 14 serves to evenly mix the hydrogen intermittently discharged by the exhaust pipeline and air so as to reduce the concentration of hydrogen.

[0031] A plurality of cooling fins are arranged along the hydrogen exhaust pipeline 9, in the section from the hydrogen outlet valve 3 to the inlet of the reservoir 61, on the outer wall of the gas-liquid separating reservoir 6 or on the inner wall of the reservoir 61.

[0032] In the present embodiment, the reservoir 61 has a volume sized according to practical needs and the range may be chosen from 0.5-20 L in order to ensure storage of exhaust gas from several rounds of discharge.

[0033] As shown in FIG. 2, the disclosed means is controlled as below:

1) opening the hydrogen inlet valve 2 and keeping the hydrogen inlet pipeline 8 unobstructed, while keeping the hydrogen outlet valve 3, the check valve 5, the hydrogen circulating pump 4 and the ventilation valve 7 closed, so that stacks of the fuel cell 1 start to react;
2) during a venting cycle T0 of the electrochemical reaction of the stack, opening the hydrogen outlet valve 3 to enter the means into its venting state, (between adjacent said venting states is one said venting cycle of the electrochemical reaction of the stack, and in the same venting cycle of the electrochemical reaction of the stack, the hydrogen outlet valve 3 opens for one or more times with a constant interval therebetween (i.e., a round of the venting state), while the hydrogen circulating pump 4 and the check valve 5 open for only one time (for a duration T2). According to the present embodiment, in the same venting cycle of the electrochemical reaction of the stack, the hydrogen outlet valve 3 has an opening frequency equal to 1-10 times of the opening frequency of the hydrogen circulating pump 4). After exhaust gas containing water, nitrogen and hydrogen enters the reservoir 61 and when the pressure of the exhaust gas as detected by the pressure sensor 611 is higher than a preset pressure upper limit, opening both the hydrogen circulating pump 4 and the check valve 5 simultaneously to draw the hydrogen in the reservoir 61 back to the hydrogen inlet pipeline 8;
3) when the concentration of nitrogen in the reservoir as measured by the nitrogen concentration meter 612 is higher than a preset nitrogen concentration threshold or when a water level as measured by the level gauge 621 is higher than a present water level threshold, opening the ventilation valve 7 to discharge the separated liquid water and redundant nitrogen and closing the ventilation valve 7 upon clearance (for a duration T3); and
4) when the pressure of exhaust gas as detected by the pressure sensor 611 is lower than a preset pressure lower limit, closing the hydrogen circulating pump 4 and the check valve 5, and starting control of the next venting cycle of the electrochemical reaction of the stack.

[0034] The present invention uses repeated, short, equal-duration opening of the hydrogen outlet valve 3 to evenly discharge the exhaust gas as the product of the reaction of the stack to the reservoir 61, where the exhaust gas is collected, buffered and stored. In this way, the check valve 5 and the hydrogen circulating pump 4 do not have to open and close along with the hydrogen outlet valve 3 every time, thereby increasing the service life and facilitating central detection and control. In the present embodiment, the opening duration T1 of the hydrogen outlet valve 3 is typically but not limited to 0.1-0.15 sec., and the opening frequency is typically but not limited to 1-10 times.