FUEL PRESSURE REGULATOR, METHOD OF REGULATING FUEL PRESSURE AND METHOD OF MEASURING A VOLUME OF FLUID FLOW
20230161362 · 2023-05-25
Inventors
Cpc classification
G05D7/0647
PHYSICS
Y02E60/50
GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
G05D16/2033
PHYSICS
International classification
Abstract
A fuel cell comprising a fuel pressure regulator apparatus on a fuel input line of the fuel cell, the apparatus comprising a first and a second valve connected in series by a fluid flow path defining an open volume between the two valves a pressure monitor device downstream of the second valve; and a controller connected to each valve for opening and closing each valve in a pulsed manner.
Claims
1. A fuel cell comprising a fuel pressure regulator apparatus on a fuel input line of the fuel cell, the apparatus comprising: a first and a second valve connected in series by a fluid flow path defining an open volume between the two valves; a pressure monitor device downstream of the second valve; and a controller connected to each valve for opening and closing each valve in a pulsed manner; wherein the valves are normally closed solenoid valves; and wherein the controller is configured to open the second valve only when the first valve is closed.
2. A fuel cell as claimed in claim 1, further comprising a fuel line having a high-pressure side connected to an input of the first valve and a low-pressure side connected to the output of the second valve.
3. A fuel cell as claimed in claim 1, wherein an output of the first valve is connected to an input of the second valve by the fluid flow path, the fluid flow path defining a fixed volume between the valves.
4. A fuel cell as claimed in claim 1, wherein the controller is configured to control both valves in a pulse-width modulated manner.
5. A fuel cell as claimed in claim 1, wherein the fluid flow path is formed as a fluid flow channel within a substrate.
6. A fuel cell as claimed in claim 2, wherein the high-pressure side and low-pressure side are formed at least partially as fluid flow channels within a substrate.
7. A fuel cell as claimed in claim 6, wherein the valves are disposed on a surface of the substrate.
8.-10. (canceled)
11. A fuel cell as claimed in claim 1, wherein the volume is 0.1-5 cm.sup.3.
12. A fuel cell as claimed in claim 1, wherein the fluid is a gas.
13. A fuel cell as claimed in claim 1, wherein the apparatus decreases the pressure of the fuel by at least 5 fold.
14. A fuel cell as claimed in claim 1, wherein the valves undergo between 120 and 1200 valve opening an closings per minute.
15. A fuel cell as claimed in claim 1, wherein the fuel cell has greater than 50 mL of fuel flow per minute and; a power rating of between 8 W and 100 W.
16. (canceled)
17. A method of regulating fuel pressure in a fuel cell comprising: flowing a fuel through a fluid flow path defining a volume between a first and a second valve connected in series where the output of the first valve directly inputs to the input of the second valve and wherein closed solenoid valves the valves are normally; monitoring the pressure of the fuel downstream of the second valve; and controlling each valve by opening and closing each valve in a pulsed manner, wherein the second valve is only opened when the first valve is closed.
18. A method as claimed in claim 17, comprising controlling both valves in a pulse-width modulated manner.
19. (canceled)
20. A method according to claim 17, wherein the time gap between the closure of one valve and the opening of the other is less than 100 ms.
21. (canceled)
22. A method according to claim 17, wherein the pulse time of each valve is between 1 ms and 15 ms per valve or, wherein the time to open and close both valves is between 50 ms and 500 ms, or wherein the valves undergo between 120 and 1200 valve opening and closings per minute.
23. (canceled)
24. A method according to claim 17, wherein the method decreases a pressure of the fuel by at least 5 fold.
25. (canceled)
26. A method according to claim 17, wherein the fuel has greater than 50 mL of fuel flow per minute and a power rating between 8 W and 100 W.
27. (canceled)
28. The method according to claim 17, wherein the method further comprises measuring a volume of fluid flow, the method comprising: controlling each valve by opening and closing each valve in a pulsed manner; and counting a number of opening or closing events of the first and second valve.
29. A method as claimed in claim 28, comprising measuring a pressure in the volume between the first and second valves.
30. (canceled)
Description
[0044] Specific embodiments of the invention will now be described by reference to the accompanying drawings, in which:
[0045]
[0046]
[0047]
[0048]
[0049]
[0050]
[0051]
[0052] The present techniques will be described more fully hereinafter with reference to the accompanying drawings. Like numbers refer to like elements throughout.
[0053]
[0054] The fuel tank 12 is a storage for the fuel. The fuel tank 12 is a pressurised fuel storage unit, for example a bottle or canister.
[0055] The fuel line 14 is a line or passage e.g. a pipe to bring or transport fuel from the fuel storage to the valves. The fuel line 14 inputs the fuel to the valves. The fuel line 14 may be considered to continue, or it may be considered that a second fuel line begins after the solenoid valves 16, 18 to take the fuel to its destination, e.g. to input the fuel to a fuel cell.
[0056] The flow downstream 24 of the regulator 10 takes fuel to a source, which could be to a fuel consumer, for example a fuel cell or a combustion engine.
[0057] The controller 26 controls the opening and closing of the valves 16, 18. The controller 26 is shown in
[0058] A downstream pressure sensor (not shown) can measure the pressure of the fuel and adjust valves 16, 18 opening and closing or firing parameters according to the pressure of the fuel. The downstream pressure sensor may be in communication with the controller(s) 26, and provide feedback to regulate the opening of the valves 16, 18. The downstream pressure sensor may have a predetermined pressure threshold, and will trigger the regulator valves to open if pressure drops below this threshold pressure. In a system dealing with fuel dropping from 10 bar to between 0.2 and 0.6 bar, the predetermined pressure threshold may be set to 0.3 bar.
[0059]
[0060] The metal block 22 comprises fluid flow channel comprising several distinct sections. The two solenoid valves 16, 18 may be considered to intersect this flow channel through the block 22 and can act to regulate the pressure of the fuel flow along the fuel path as a whole.
[0061] Because the system acts to reduce the pressure, before the first solenoid 16 is a “high pressure side” 28 of the system, and after the second solenoid 18 is a “low pressure side” 30 of the system.
[0062] Fuel flow begins on the high pressure side 28 of the system. The fuel line 14 is connected to an input 32 of the first valve 16, so fuel from fuel line 14 can flow into the first valve 16. The output 34 of the first valve 16 is then connected to the volume 20 between the two valves 16, 18. The volume 20 is then connected to the input 36 of the second valve 18. The second valve 18 has an output 38 connected to the downstream flow 24, so fuel can flow downstream 24 out of the regulator system 10. The flow out of the second valve 18 is on the low pressure side 30 of the system.
[0063] “Normally closed” refers to valves which are closed when there is no power supplied to them. When power is supplied to them, the valves are opened. ‘3/2 solenoid valves’ as shown in
[0064] In operation, when the solenoid electric coil 15 of each valve is de-energized, the valve (16 or 18) shuts off the flow of fuel to the intended destination. When the solenoid electric coil 15 is energized the flow is open, and then fuel will be allowed to flow through to the intended destination. When de-energised, an output of each valve 16, 18 is connected to a valve exhaust port (not shown in figure), which becomes blocked once the coil is energised. When energised, the valves 16, 18 will link fuel inputs 32, 36 and fuel outputs 34, 38 in each valve 16, 18 to allow fuel to flow through and out of the valves 16, 18.
[0065] Thus, fuel flow is enabled only when the solenoids 16, 18 are energised or triggered and thus opened. When normally closed they block the flow of fuel. When the controller 26 triggers the first solenoid 16 to open (i.e. when the electrical coil 15 is stimulated), fuel will flow from the high-pressure side 28 through the input 32 and output 34 of the first valve 16. The volume 20 between the valves 16, 18 will then be filled with fuel. When the controller 26 triggers the second solenoid 18 to open the fuel will flow out of the volume 20, through the input 36 and output 38 of the second valve 18, into the low pressure side 30 of the system 10 and downstream 24 of the pressure regulation system 10. The fuel will flow through the regulator system 10 in this manner because the overall flow through the system described herein is from higher pressure 28 to lower pressure 30.
[0066] In this manner, the action of the two valves 16, 18 reduces the pressure of the fuel. As a valve opens the act of the fuel flowing into the following space (whether that be a continuing fuel line 24, or the volume 20 between the two valves) reduces fuel pressure. In particular, the fuel flowing into the volume 20 between the valves 16, 18 reduces the pressure.
[0067] In an exemplary embodiment, in operation the first valve 16 and second valve 18 are not stimulated to open at the same time, so there is never a fully open flow path from the high-pressure side 28 to the low-pressure side 30. A fixed volume 20 between solenoids acts as a control volume between high-pressure 28 and low-pressure 30 sides.
[0068] In a further exemplary embodiment, in operation the first valve 16 and second valve 18 may be stimulated to open at the same time, but only for a relatively short period of time. The overlap in the two valves opening may be a relatively small percentage of the total opening time for either valves, for example less than 10% of the time either of the valves is open. In an exemplary embodiment, where the period (time for both valves to open and close) is around 50 ms, each valve is open for around 20 ms and the overlap time where both valves are open is around 4 ms.
[0069] Solenoid valves are capable of acting in a pulsed manner, opening and shutting quickly enough to allow fuel to pass through a valve but to also reduce the pressure of the fuel as the fuel passes through a valve. The pulsed manner of operation reduces the power usage of solenoid valves, as less power is needed than to keep valves open the whole time, as with the solenoid valves used in the prior art fuel cells. Thus, the valves 16, 18 described herein can be pulse-width modulated. The lifetime of solenoid valves means they are especially suited for use in these pressure regulation systems, opening and closing a sufficient number of times without needing to be serviced in order to last the lifetime of a fuel cell.
[0070] In the embodiments of the invention shown in
[0071]
[0072] A line representing the first valve (e.g. solenoid 16) is labelled as 42 and is shown with an unbroken line, the line representing the second valve (e.g. solenoid 18) is labelled as 44 and is shown with a dashed/broken line. The various times and parameters that are relevant to the control of the system are shown and labelled; a ‘duty cycle’ 46 of the first valve 16, a ‘cycle lag’ 48 and a ‘period’ 50 are shown. Time is represented on the x axis, to represent the passage of time as the two valves 16, 18 open and close. The opening and closing of the valves 16, 18 is represented on the y axis.
[0073] In this exemplary embodiment of the invention, the first solenoid valve 16 opens first, and the duty cycle 46 of this is labelled. The ‘cycle lag’ 48, between the opening of the first valve 16 and the opening of the second valve 18 is also show. The period 50, the time between the opening of the first valve 16 the first time and the opening of the first valve 16 the second time is also shown.
[0074] The first valve 16 is shown to open and then also close, before the first opening and subsequent closing of the second valve 18. After the second valve 18 closes the first valve 16 then opens again, for a second time shown on the graph. The second closing of the first valve 16 is not shown on the graph.
[0075] The duty cycle 46 for each valve (16, 18) is the duration of time a valve stays open. The cycle lag 48 is the difference in time between the opening of the first valve 16 and the second valve 18. The period 50 is the duration between opening events for a single valve, i.e. just for the first valve 16 or the second valve 18 acts alone. In order to ensure there is no direct flow from the high pressure side 28 to the low-pressure side 30, the cycle lag 48 time must not exceed the duty cycle 46 time, otherwise both valves 16, 18 would be open at the same time. Fuel would be free flowing and pressure would not be regulated if that were to happen. If both valves are to be open at the same time, it must only be for a period of time relatively short to the open time of both or either valves. This overlap time will allow a known volume of fuel to free flow through the regulator. This can be accounted for when calculating the operation parameters of the regulator and method of operation.
[0076] Between the two solenoid valves 16, 18 in the systems and methods of the present invention there is the known volume 20. The amount of fuel that fills the volume will depend on the duty cycle 46 of the valves 16, 18, or until the void equilibrates pressure with the upstream fuel.
[0077] Thus, the most effective way to control the flowrate of fuel is by controlling or setting the period 50. By reducing the period 50, flowrate will increase, and vice-versa. Moreover, by minimising the size of the volume 20, the pressure of the fuel can be more easily controlled, as fuel can fill the volume 20 between the two valves 16, 18 in smaller increments.
[0078] The larger the volume 20 the lower the pressure of the fuel will be, or the lower the spike in the pressure in the volume 20 when the fuel flows in, thus a longer cycle time will be needed to equilibrate the fuel pressure. The smaller the volume of the volume 20 is kept, the quicker the volume will equilibrate with the upstream side, and hence the duty cycle 46 can be kept low. Furthermore, a smaller volume 20 allows the incremental pressure increase of the fuel downstream of the regulator per cycle to be lower and hence allow a less varied, spiked or erratic pressure of the fuel during operation of the system. Furthermore, if the cycle time of both valves opening and closing is longer, the overall flow of fuel through a system is slower, and the pressure of the fuel will be more varied as it passes through the system. For example, when the volume is 0.1 cm.sup.3, when this is pressurised to 10 Bar it is equivalent of 1 cm.sup.3 of gas. Operators and users of such regulators and methods will be able to calculate the volume of gas desired to pass through the system, and design the system or method parameters accordingly. Parameters such as the volume will be known by any regulator (e.g. 26) controlling the operation of the valves.
[0079] In an exemplary embodiment of the invention, the cycle is as follows: the first solenoid 16 fires with an 8 ms pulse, there is a 20 ms pause and then the second solenoid 18 fires with an 8 ms pulse. Then 50 ms from the first solenoid 16 firing the downstream pressure of the fuel is measured and if the pressure is below a predetermined threshold then the valve opening cycle is re-triggered. If the pressure is above a predetermined threshold then the valves may not be triggered to open. The downstream pressure monitor will continue to measure the pressure and when the pressure decreases or drops below the predetermined pressure then the valve opening cycle is re-triggered. This allows monitoring of the downstream pressure so the system can account for variations and can control the flow of fuel.
[0080] In an exemplary embodiment of the invention there is a duty ratio of 0.1-0.5, with a cycle lag about 20-50% of the duty cycle.
[0081] The timings in
[0082] As described above, when the first solenoid 16 opens, the volume 20 between the solenoids 16, 18 is filled with the upstream fuel. The amount of fuel that fills the volume 20 will depend on the duty cycle 34 of the first valve 16, or until the void equilibrates pressure with the upstream fuel. When the second solenoid 18 triggers, the fuel from the volume 20 fills the downstream side 24, i.e. the fuel-cell side.
[0083] An advantage of the presently described system is that the timing and cycles described herein are variable whilst the system is in operation, dependent on feedback from the system. The downstream pressure sensor may measure the pressure of the fuel and adjust the valve opening and closing or firing parameters. This allows a greater degree of fuel flow control than previously offered.
[0084]
[0085] The line representing the first valve 16 is again labelled as 42 and is shown with an unbroken line, the line representing the second valve 18 is labelled as 44 and is shown with a dashed/broken line. The various times and parameters that are relevant to the control of the system are also shown; the ‘duty cycle’, 46 of the first valve 16, the ‘cycle lag’, 48 and the ‘period’, 50 are shown. Time is represented on the x axis, to represent the passage of time as the two valves 16, 18 open and close. The opening and closing of the valves 16, 18 is represented on the y axis.
[0086] In
[0087]
[0088] The period in seconds of the operation of the two solenoid valves 16, 18 is shown on the x axis of the graph of
[0089] Flow is enabled only when the solenoids 16, 18 are triggered, hence flowrate can be highly non-linear, particularly for longer periods. In order to determine a representative average flowrate for each period condition, an inverted cylinder was used to measure the flowrate out of the metal block. A minimum of one litre of gas or three minutes of operation was observed in order to measure an average gas flow rate whilst minimising error in measurement. For a two second solenoid period, this minimum restriction represents ninety solenoid triggering events.
[0090] Generally, higher flow rates are shown at higher pressures, as to be expected. Set ups with a reduced period also results in an increased flow rate, at all pressures.
[0091] From this data it is evident that there is a more or less linear relationship at periods of 1 second and above, simplifying the control of flow at low flow rates. Below 1 second there are fluid dynamic effects which cause de-linearity of this relationship. However, there is scope to decrease the period further, subject to the limitations of the solenoid hardware) in order to allow increased flowrates.
[0092]
[0093] The pressure is recorded by an in-line pressure transducer which was also controlling the feedback loop triggering the solenoids; the solenoids are triggered when a lower pressure threshold is reached, until the pressure is topped up to a higher threshold value. The recording of the solenoid trigger events was enabled by measuring the voltage of the solenoids which again were being triggered by the feedback control system. The pressure is being measured after the second inlet solenoid and before the fuel cell.
[0094] Outlet solenoids are also present in the systems demonstrated in
[0095] The x axis of the graphs show time in seconds, and the two y axis show i) the solenoid voltage (three solenoids shown, two inlet solenoid—solenoid 1 and solenoid 2—and one outlet solenoids which are normally closed; open when excited to 12 V) and ii) the pressure (bar) of the fuel as measured downstream from the two inlet solenoids but upstream from the outlet solenoid.
[0096] In all graphs the solenoid triggering events can be seen as the substantially vertical lines rising from the x axis, e.g. multiple events visible around 5 seconds in
[0097]
[0098]
[0099] The zoomed in cases presented are to highlight solenoid behaviour and show the pressure changes in more detail. Pressure can be seen rising and falling as described in
[0100]
[0101] It will be clear to one skilled in the art that many improvements and modifications can be made to the foregoing exemplary embodiments without departing from the scope of the present technique.
[0102] For example, in a further aspect of the invention there is provided a cell assembly incorporating a system as described above, with a fuel source to deliver fuel to the control system, and a fuel cell.
[0103] Preferably, the fuel enters the system at a pressure of between 2 and 10 bar. Preferably, the fuel leaves the system at a pressure of between 0.2 to 0.6 bar. However, in systems scaled larger or smaller, the system, apparatus and methods of the present invention could be used with fuels of higher and lower pressures.
[0104] Preferably, the fuel cell has a power output in the range of 10-100 W.
[0105] A fuel pressure regulator of the present invention may be connected to a downstream sensor. The sensor may take a measurement downstream of the valves, measuring a pressure of the fuel after it has flowed through the valves. This can then be fed back into the regulator to control the opening and closing of the valves, in particular in order to further reduce or allow an increase in pressure of the fuel. The downstream sensor may be a pressure sensor, such as those known to those skilled in the art. A valve regulator capable of controlling the opening and closing of valves would also be known to those of skill in the art.
[0106] The measurement or counting of the fluid can be made more accurate by incorporating a measurement device into the system. The measurement device can intersect the volume between solenoids. The measurement device could be a pressure sensor. Using a pressure sensor would depend on the upstream and downstream pressure from the valves. Knowing this and knowing using a pressure sensor to measure the pressure in the volume would mean the flow amount can be calculated.
[0107] A pressure sensor used to measure the pressure in the volume between the two valves could replace other pressure sensors usually found in such systems, e.g. downstream pressure sensors as part of a regulator as described above.
[0108] With the diagram regulators used in the prior art, there is no indication of how much fuel has passed through the regulator(s). It is possible to back-count from the fuel cell, or measure how much fuel has left the fuel storage unit, but this doesn't accurately account for losses on the way.
[0109] This information could be communicated to a user of such a system or a method, for example via a fuel cell control system. This can indicate to a user when a fuel storage unit is running low on fuel, or help calculate how efficient a system is being.
[0110] Such calculations are possible once the system has equilibrated, because the amount of fuel passing through is known once the system reaches equilibrium. The time taken to equilibrate will depend on a number of factors such the pressures of the fuel before and after the valves, fuel types and the physical parameters of the system.
[0111] The methods and systems described herein may use more than two valves in series to regulate the fuel pressure, for example, 3, 4, 5, 6 or more valves in series. In particular in larger systems or systems operating at a higher pressure than a small-scale fuel cell, there may be particularly advantages of using 3 valves in series to regulate the pressure in the system. More than 2 valves may be particularly suitable when there is no pressure regulator on the fuel source, or when the fuel is stored at a high pressure. For example, in a system where the fuel is stored at 300 bar pressure, reducing the pressure using 3 valves may be advantageous.
[0112] Systems and methods in accordance with the invention can be used in fuel-cell assemblies of differing power output capabilities. The fuel cells utilising such a system could be used in fuel cells capable of, for example, 200 W of power output, of 150 W power output, of 100 W power output, of 90 W power output, of 80 W power output, of 70 W power output, of 60 W power output, of 50 W power output, of 40 W power output, of 30 W power output, of 20 W power output, of 10 W power output, of 5 W power output. This is the maximum power output of the fuel cells, cells can be set to the power output required as necessary.
[0113] Systems and methods in accordance with the invention have particular advantages when used with 200 W or below fuel cells. Smaller fuel cells see particularly advantages due to the power saving by using these systems and methods. For example, a 2 W saving is in percentage terms less of an energy saving on a 1000 W power output fuel cell when compared to a 100 W power output fuel cell, but it is still a saving and may be worth incorporating depending on requirements.
[0114] The valves of the systems and methods of the present invention use under 100 mW of power, or under 90 mW of, or under 80 mW of power, or under 70 mW of power, or under 60 mW of power, or under 50 mW of power, or under 40 mW of power. Valves vary in size from 10 mL to 20/25 mL, the orifice size of a valve for use in the fuel cells as described herein is typically about 0.5 mm in diameter.
[0115] Pulse width-modulated solenoid valves can go through 500 million cycles, which is more than enough to last the 3 to 5 year inspection/replacement cycle that diaphragm valves would go through.
[0116] Also, with two valves in series, advantageously each can be isolated for testing/diagnostics to be run on a single valve at a time. This is not possible in the diaphragm valve type systems of the prior art. Systems of the present invention can include electronics running continuously or intermittently to check the movements of the (individual) valves in ordinary use. Systems can run in-line diagnostics to monitor the valves, individually or together.
[0117] Although the invention as exemplified uses hydrogen as the fuel, this valve arrangement and methods could be used with all pressurised fluids. As used herein “fluid” refers to a substance that has no fixed shape and yields easily to external pressure, for example a gas or a liquid. Fuels for use with the systems and methods as described herein are fluids. These fuels can be hydrogen or a hydrogen-containing mixture, or a hydrocarbon or hydrocarbon derivative. Fuels could be other gaseous fuels, such as methane or propane. Fuels could be other gaseous fuels, such as methane or propane and fluids include oxidants such as air and oxygen.
[0118] The systems and methods can be used with pressurised fuel storage units or containers, as are well known in the art. The fuel can be stored in a pressurised storage unit, for example a bottle or canister. These can be, for example at a pressure of between 700 and 10 bar. In particular the fuel storage units can be suitable for use with fuel cells as described herein, i.e. at a pressure of between 150 and 350 bar.