WO2004046841A1 - Inspirated pressure control system - Google Patents

Inspirated pressure control system Download PDF

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Publication number
WO2004046841A1
WO2004046841A1 PCT/CA2003/001787 CA0301787W WO2004046841A1 WO 2004046841 A1 WO2004046841 A1 WO 2004046841A1 CA 0301787 W CA0301787 W CA 0301787W WO 2004046841 A1 WO2004046841 A1 WO 2004046841A1
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WO
WIPO (PCT)
Prior art keywords
pressure
fluid
valve
actuating
target
Prior art date
Application number
PCT/CA2003/001787
Other languages
French (fr)
Inventor
Gordon John Lamont
Chad Comeault
Roger Harper
Original Assignee
Greenlight Power Technologies, Inc.
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Greenlight Power Technologies, Inc. filed Critical Greenlight Power Technologies, Inc.
Priority to AU2003283165A priority Critical patent/AU2003283165A1/en
Publication of WO2004046841A1 publication Critical patent/WO2004046841A1/en

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Classifications

    • GPHYSICS
    • G05CONTROLLING; REGULATING
    • G05DSYSTEMS FOR CONTROLLING OR REGULATING NON-ELECTRIC VARIABLES
    • G05D16/00Control of fluid pressure
    • G05D16/14Control of fluid pressure with auxiliary non-electric power
    • G05D16/16Control of fluid pressure with auxiliary non-electric power derived from the controlled fluid
    • G05D16/163Control of fluid pressure with auxiliary non-electric power derived from the controlled fluid using membranes within the main valve
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/04Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
    • H01M8/04082Arrangements for control of reactant parameters, e.g. pressure or concentration
    • H01M8/04089Arrangements for control of reactant parameters, e.g. pressure or concentration of gaseous reactants
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/04Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
    • H01M8/04082Arrangements for control of reactant parameters, e.g. pressure or concentration
    • H01M8/04186Arrangements for control of reactant parameters, e.g. pressure or concentration of liquid-charged or electrolyte-charged reactants
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30Hydrogen technology
    • Y02E60/50Fuel cells

Definitions

  • the present invention relates generally to a pressure control system. More particularly, the present invention relates to a pressure control system for low pressure operation.
  • a known pressure control system comprises an unloading type flexible element pressure regulator and a piloting system.
  • the pressure regulator is disposed in the process fluid stream line and in operation, allows the process fluid to flow through a chamber thereof disposed on one side of the flexible element, e.g. a diaphragm.
  • a pilot controller senses the pressure at the point where the pressure of the process fluid stream is to be accurately controlled, and correspondingly controls the pressure of another chamber on the other side of the flexible element of the pressure regulator, thereby eventually balancing the pressure on both sides of the flexible element.
  • By manually adjusting the preset pressure of the pilot controller the pressure of the process fluid stream at the desired point can be controlled.
  • Such pressure regulator and the piloting system and the way they are operated are commercially available from, for example, Mooney Controls.
  • a pressure control system for controlling the pressure of a process fluid stream at a certain location, comprising:
  • Figure 1 is a schematic view of a known pressure control system
  • Figure 2 is a schematic view of an embodiment of a pressure control system according to the present invention.
  • Figure 3 is an enlarged portion of the schematic view of Figure
  • Figure 4 is an enlarged portion of the schematic view of Figure
  • Figure 5 is an enlarged portion of the schematic view of Figure
  • Figure 6 is an enlarged portion of the schematic view of Figure
  • Figure 7 shows an end view of a portion of the regulator of
  • Figure 8 shows test results of pressure at a fuel cell stack inlet with various process fluid flows using the pressure control system of Figure
  • a known pressure control system is shown generally at 10 in
  • the pressure control system 10 comprises an unloading type flexible element pressure regulator 20 and a piloting system.
  • the pressure regulator 20 is disposed in the process fluid stream line 40 and in operation, allows the process fluid to flow through a chamber 24 thereof disposed on one side of the flexible element, e.g. a diaphragm 28.
  • a divider 22 is disposed in the chamber 24 to adjust the pressure therein. The divider 22 initially abuts against the flexible element 28 and hence prevents the process fluid from flowing through the chamber 24. As the process fluid is continuously fed into the chamber 24, pressure in the chamber 24 increases and the diaphragm 28 is lifted. This permits the flow of the process fluid through the chamber 24.
  • a pilot controller 30 senses, via a sense line 60, the pressure at the point 50 where the pressure of the process fluid stream is to be accurately controlled, and correspondingly controls, via a control line 80, the pressure of another chamber 26 on the other side of the flexible element 28 of the pressure regulator 20, thereby eventually balancing the pressure on both sides of the flexible element 28, at a desired pressure.
  • a further line 32, including an orifice or throttle 34 is connected to the pilot controller 30, and an exhaust line 36 is also provided.
  • fluid is supplied through the line 32 and orifice 34 to the pilot controller 30.
  • a pressure is sensed by the controller 30, it is maintained in a closed position, so that flow from the line 32 is directed to the line 80 to maintain the pressure regulator 20 closed, thereby to increase the pressure in the line 40.
  • this pressure is applied through the sense line 60 to the pilot controller 30 to open the controller against the action of the spring indicated therein. This permits at least part of the flow from line 32 to be exhausted through the exhaust line 36 to the outlet of the pressure regulator 20. Consequently, the pressure on the diaphragm 28 is reduced, permitting the regulator 20 to open, thereby to reduce the pressure in the line 40.
  • a pressure control system according to the present invention is shown generally at 110 in Figure 2.
  • the pressure control system 110 has a pressure regulator 112, an inspirator 114, a primary (low pressure) pilot 116, and a secondary (higher pressure) pilot 118.
  • the pressure regulator 112 is mounted in a process fluid line
  • the regulator 112 has an inlet port 120a in fluid communication with an upstream line 102a of the process fluid line 102, and an outlet port 120b in fluid communication with a downstream line 102b of the process fluid line 102.
  • the regulator 112 is further provided with a flow channel 122 extending between the inlet and outlet ports 102a, 102b and with a closure means 124 in the flow channel 122.
  • the closure means 124 is variably adjustable between a fully closed position, in which the ports 102a and 102b are fluidly isolated from each other, and a fully open position in which a maximum rate of flow is permitted through the flow channel 122.
  • the closure means 124 comprises a sealing surface 126 attached to a flexible actuating diaphragm 128.
  • the diaphragm 128 serves as an actuator for advancing the sealing surface 126 towards, or retracting the sealing surface 126 away from, an engagement surface 130 provided on a divider element 132.
  • the divider element 132 can be in the form of a fixed wall extending into the flow channel 122.
  • the actuating diaphragm 128 can move in response to a pressure differential across the thickness of the diaphragm 128. Accordingly, in the embodiment illustrated, one face 129a of the diaphragm 128 (i.e. the face with the sealing surface 126) partially defines the flow channel 122, and the opposite face 129b of the diaphragm 128 partially defines a control chamber 136.
  • the position of the actuating diaphragm 128, and hence of the closure means 124 can be controlled, and moved between a fully lowered position 128a and a fully raised position 128b (shown in phantom in Figure 3), corresponding to fully closed and fully open positions of the valve closure means 124.
  • the pressures in the flow channel 122 and control chamber 136 are equal, and the diaphragm 128 is substantially stationary.
  • the pressure in the control chamber 136 is adjusted by forcing actuator fluid into, or evacuating actuator fluid from, the chamber 136 via a pressure control line 138 that extends between the chamber 136 and the inspirator 114 ( Figure 2). More particularly, the inspirator 114 has, in the form of a venturi, a converging inlet 140, a diverging outlet 142, and a throat 144 between the inlet 140 and outlet 142.
  • the pressure control line 138 extends between the control chamber 136 and the throat 144 of the inspirator 114 ( Figure 4).
  • the inspirator 114 receives a flow of actuator fluid at its inlet
  • the fluid in the supply line 146 is supplied at a relatively constant, higher than target, pressure from a fluid source independent of the process fluid in line 102.
  • the flow of fluid through the inspirator 114 is accelerated in the inspirator, so that a pressure drop is generated at the throat 144 of the inspirator.
  • the pressure drop can generate suction in the control chamber 136 to lift the diaphragm 128 and open the closure member 124.
  • the venting is restricted, fluid entering the inlet 140 can be directed into the chamber 136, thereby urging the diaphragm 128 downwards and closing the closure member 124.
  • the primary pilot 116 has a control portion 150 and a valve portion 152, which are in fluid isolation from each other.
  • the valve portion 152 has an inlet port 154, an outlet port 156, and a valve member 158 between the inlet port 154 and outlet port 156.
  • the inspirator vent line 148 connects the outlet 142 of the inspirator 114 to the inlet port 154 of the primary pilot 116.
  • the outlet port 156 is open to atmosphere.
  • the valve member 158 can move among a fully closed position, a fully open position, and various degrees of partially open positions. In this way, the valve member 158 controls the flow of fluid from the inlet port 154 to the outlet port 156, and hence, the valve portion 152 of the primary pilot 116 controls the flow of fluid from the outlet 142 of the inspirator 114 to atmosphere.
  • the control portion 150 of the primary pilot 116 adjusts the position of the valve member 158 of the primary pilot 116.
  • the control portion 150 has a target pressure chamber 160 and a sensed pressure chamber 162 that are separated from each other by a primary pilot diaphragm 164.
  • the primary pilot diaphragm 164 has a target pressure face 165a exposed to the target pressure chamber 160, and a sensed pressure face 165b exposed to the sensed pressure chamber 162.
  • a pressure adjustment spring 163 is housed within the target pressure chamber and exerts a force against the target pressure face 165a of the diaphragm 164, as does any fluid pressure in the target pressure chamber 160.
  • the diaphragm 164 By changing the relative pressures in the target and sensed pressure chambers 160, 162, the diaphragm 164 is moved towards one of the chamber 160, 162 dependent on the pressure differential and the load set on the spring 163, which can be adjustable.
  • the valve member 158 is connected to the diaphragm 164 by, for example, a shaft 166 and a lever 168 pivotally mounted as shown, so that movement of the diaphragm 164 adjusts the position of the valve member 158. More particularly, a downward movement of the diaphragm 164 (movement towards the sensed pressure chamber 162) closes the valve member 158, and upward movement of the diaphragm 164 (towards the target pressure chamber 160) opens the valve member 158.
  • the spring 163 is relatively soft and the surface area of the faces 165a and 165b of the diaphragm 164 are relatively large so that the diaphragm 164 has greater sensitivity to small pressure differentials across the diaphragm 164.
  • control input 170 can be a pressurized supply of fluid regulated by, for example, but not limited to, an electronic pressure regulator, and connected to a target port 172 of the target pressure chamber 160 via a control line 174.
  • a sense line 180 extends from a sense port 182 of the sensed pressure chamber 162 to an orifice in the line 102 at the point 178. In this way, the pressure of the fluid stream in the line 102 at the point 178 is reflected by the pressure in the sensed pressure chamber 162.
  • the regulator 112 may be caused by an increase in fluid flow through the regulator 112 (i.e. an increase in fluid consumption by the system).
  • the higher pressure in the target pressure chamber 160 of the pilot 116 presses the diaphragm 164 towards the sensed pressure chamber 162, which therefore moves the valve member 158 to a more closed position.
  • the actuator diaphragm 128 advances towards the engagement surface 130 of the divider 132, thereby restricting flow through the flow channel 122 of the regulator 112 and increasing the pressure at the sensing point 178.
  • An increase in the sensed system pressure may be caused by a decrease in fluid flow through the regulator 112 (i.e. a decrease in fluid consumption by the system).
  • the higher pressure in the sensed pressure chamber 162 pushes the pilot diaphragm 164 towards the target pressure chamber 160, so that the valve member 158 is moved to a more open position.
  • This increases the flow of fluid from the outlet 142 of the inspirator 114, which in turn reduces the pressure in the pressure control line 138 and the pressure control chamber 136 of the regulator 112.
  • the diaphragm 128 retracts away from the engagement surface 130 of the divider 132, which increases flow through the channel 122 and decreases the pressure at the sensing point 178.
  • the pressure control system 110 reacts to counteract the pressure deviation.
  • a supply of actuator fluid through the inspirator supply line 146 can be provided by an independent (or auxiliary) fluid supply 188 that is passed through the secondary (higher pressure) pilot 118.
  • the actuator fluid supply 188 can be a supply of any fluid that is isolated from the process fluid line 102, and is preferably supplied at a pressure greater than the target pressure input 170.
  • the secondary pilot 118 has a control portion 190 and a valve portion 192, which are fluidly isolated from each other.
  • the valve portion 192 has an inlet port 194 and an outlet port 196, and a valve member 198 between the inlet port 194 and outlet port 196.
  • An auxiliary supply line 199 connects the auxiliary fluid supply 188 to the inlet port 194 of the auxiliary pilot 118.
  • the outlet port 196 is connected to the inspirator supply line 146.
  • the valve member 198 can move among a fully closed position, a fully open position, and various degrees of partially open positions, so that the valve portion 192 of the secondary pilot 118 controls the flow of fluid from the auxiliary fluid supply 188 to the inlet 140 of the inspirator 114.
  • the control portion 190 of the secondary pilot 118 adjusts the position of the valve member 198 of the secondary pilot 118.
  • the control portion 190 has a target pressure chamber 200 and a sensed pressure chamber 202 that are separated from each other by a secondary pilot diaphragm 204.
  • the secondary pilot diaphragm 204 has a target pressure face 205a exposed to the target pressure chamber 200, and a sensed pressure face 205b exposed to the sensed pressure chamber 202.
  • a pressure adjustment spring 203 is housed within the target pressure chamber 200 and exerts a force against the target pressure face 205a of the diaphragm 204, as does any fluid pressure in the target pressure chamber 200.
  • the force of the spring 203 can be adjusted by turning an adjustment screw 207 to change the preload on the spring 203.
  • the valve member 198 can be connected to the diaphragm 204 by, for example, a shaft 206, so that movement of the diaphragm 204 adjusts the portion of the valve member 198.
  • the spring 203 is relatively stiff and the surface area of the faces 205a and 205b of the diaphragm 204 are relatively small (compared to those of the primary pilot 116).
  • control pressure input 170 can be in fluid communication with the control pressure input 170. More specifically, the control (or target) pressure input 170 can be in communication with the chamber 200 via a secondary pilot control line 210 connecting the control line 174 of the primary pilot 116 to a target port 212 of the chamber 200. A stabilizing needle valve 213 can be provided in the secondary pilot control line.
  • the outlet port 196 of the secondary pilot valve 118 is in fluid communication with the inspirator supply line 146.
  • a sense line 214 extends from a sense port 216 of the sensed pressure chamber 202 to an orifice in the inspirator supply line 146 between the outlet port 196 of the valve portion 192 of the secondary pilot 118 and the inlet 140 of the inspirator 114.
  • the auxiliary fluid supply 188 can be supplied to the pressure control system 110, via the line 199, at a pressure that is greater than the target pressure (which is set as desired by the target pressure input 170).
  • the fluid pressure to the outlet 196 of the secondary pilot 118 (and hence, the fluid pressure to the inlet 140 of the inspirator 114) is generally equal to the system target pressure.
  • the screw 207 By adjusting the screw 207 to increase the force on the target face 205a of the diaphragm 204, fluid at a higher pressure can be passed to the inspirator. Accordingly, a greater pressure difference can be generated across the diaphragm 128 of the regulator 112.
  • the regulator 20 is usually positioned so that the diaphragm 28 is facing vertically upwards, or in other words, the diaphragm 28 is generally horizontal having the chamber 26 above and the chamber 24 below.
  • the divider 22 is oriented generally vertically, and a partial gap or flow channel is provided between the top of divider 22 and the bottom of diaphragm 28.
  • liquid can condense and accumulate in the upstream side (left side in Figure 1) of the divider 22 causing partial blockage of the flow passage which can in turn create a significant pressure change in the gas stream. This can result in instability of pressure control and is therefore undesirable.
  • the pressure regulator 112 of the control system 110 can be rotated approximately 90 degrees around its axial direction, i.e. the direction of the process fluid stream therethrough ( Figure 7).
  • the divider 132 is disposed generally in horizontal position, and the diaphragm 128 extends in a generally vertical direction, with the flow channel 122 on one side and the chamber 136 on the other side.
  • condensed liquid can more easily flow through the flow channel 122 between the surfaces 126 and 130. This can eliminate any significant pressure change due to condensation, so that the pressure of the process gas stream can be controlled constantly at a steady level.
  • the pressure control system 110 In one application of the pressure control system 110, a fuel cell stack was placed between the pressure control point 178 in the line 102a and the inlet 120a of the pressure regulator. Test results of this example are provided hereinafter. It is to be appreciated, however, that the present system 110 can be used to control pressure of the process fluid stream at any arbitrary location along the process fluid stream line. It is also to be appreciated that the present invention can be applied in many industrial applications, where accurate control of the pressure of a process fluid stream is desirable, especially under low pressure conditions, including but not limited to a fuel cell system.
  • control pressure at inlet 170 was set at about
  • the auxiliary supply stream was provided at about 100psi.
  • the adjustment screw 207 was adjusted so that the total force exerted on the target pressure face 205a of the diaphragm 204 was equivalent to about 25psi.
  • a fluid consuming device in the form of a load cell stack was disposed in the upstream fluid line 102a, between the control point and the regulator 112.
  • Figure 4 shows test results when the present pressure control system in employed in a fuel cell system. As can be seen, although the process gas flow changes dramatically from near zero slpm to 200 slpm, the pressure of the process fluid at a certain point in the system is maintained at reasonably constant level.
  • the invention has been described in relation to a configuration where the pressure is sensed upstream from the pressure regulator 112.
  • the invention is intended for particular application with fluid cell stacks where the fluid cell stacks are interposed between the sensing port 178 and the pressure regulator 112.
  • the invention also has applicability where it is desired to control the pressure downstream from the pressure regulator 112. In this case, the operation of the first pilot valve 116 will need to be reversed. Thus, if the downstream pressure was sensed to be too high then it would be necessary to reduce the flow of fluid through the pressure regulator 112 to the downstream location.
  • valve member 158 In response to excess sensed pressure, the valve member 158 would need to moved to a more closed position thereby to reduce the flow from the inspirator 114, in turn increasing the pressure of the actuating fluid delivered through the line 138 to the pressure regulator 112, so as to tend to close the pressure regulator 112 and reduce flow of fluid through it.
  • the pilot valve 116 if the downstream pressure is sensed to be too low, then the pilot valve 116 needs to be opened so as to permit greater flow of fluid through it from the inlet port 154 to the outlet port 156. This greater flow of actuating fluid would reduce the pressure at the throat of the inspirator 114, in turn reducing the pressure applied to the pressure regulator 112, so as to let greater flow of fluid through the pressurized regulator 112, so as in turn to increase the downstream pressure.

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  • Engineering & Computer Science (AREA)
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  • Life Sciences & Earth Sciences (AREA)
  • Fluid Mechanics (AREA)
  • General Physics & Mathematics (AREA)
  • Automation & Control Theory (AREA)
  • Power Engineering (AREA)
  • Manufacturing & Machinery (AREA)
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  • Sustainable Energy (AREA)
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  • Control Of Fluid Pressure (AREA)

Abstract

A pressure control system for controlling the pressure of a process fluid, for example a gas, at a certain location includes first and second pilot valves and a pressure control element. A sensed fluid pressure is connected to the first pilot valve, this controls flow of fluid from a fluid control element. An auxilary gas or fluid supply is connected to the second pilot valve, which contols the pressure which the auxiliary fluid is supplied to the fluid control element. A pressure regulator in the process fluid line has an actuating element that responds to actuating fluid to open or close the pressure regualtor. This actuating fluid is supplied by the fluid control element. Thus, actuating fluid is supplied to the fluid control element, and the pressure of which this actuating fluid is transmited to the pressure regulator is determined by the first pilot valve.

Description

INSPIRATED PRESSURE CONTROL SYSTEM
FIELD OF THE INVENTION
[0001] The present invention relates generally to a pressure control system. More particularly, the present invention relates to a pressure control system for low pressure operation.
BACKGROUND OF THE INVENTION
[0002] In various industrial applications, it is often desirable to accurately control the pressure of a process fluid stream at a certain point in an industrial system. The process fluid can be gas, liquid, or mixture thereof. For example, in a fuel cell system or a fuel cell testing system, it is necessary to operate the fuel cell under a controlled pressure condition. A common technique is to control the pressure of a process fluid stream adjacent the inlet of the fuel cell for that process fluid stream. To this end, a pressure regulator is often utilized to control the pressure at this point. [0003] A known pressure control system comprises an unloading type flexible element pressure regulator and a piloting system. The pressure regulator is disposed in the process fluid stream line and in operation, allows the process fluid to flow through a chamber thereof disposed on one side of the flexible element, e.g. a diaphragm. A pilot controller senses the pressure at the point where the pressure of the process fluid stream is to be accurately controlled, and correspondingly controls the pressure of another chamber on the other side of the flexible element of the pressure regulator, thereby eventually balancing the pressure on both sides of the flexible element. By manually adjusting the preset pressure of the pilot controller, the pressure of the process fluid stream at the desired point can be controlled. Such pressure regulator and the piloting system and the way they are operated are commercially available from, for example, Mooney Controls.
[0004] However, it has been found that this type of pressure control system cannot meet the increasingly strict requirement in terms of accuracy and stability, when a system operates at low pressure, e.g. less than 7 psig, partly because that the pressure regulator needs a certain pressure drop across it to activate the pressure balancing mechanism and such pressure drop is often not available when pressure of the process fluid stream is extremely low.
[0005] Therefore, there remains a need for a pressure control system that accurately controls the pressure of a process fluid stream at a certain point, under a range of pressure conditions including very low pressure of the process fluid stream.
SUMMARY OF THE INVENTION
[0006] In accordance with the present invention, there is provided a pressure control system for controlling the pressure of a process fluid stream at a certain location, comprising:
BRIEF DESCRIPTION OF THE DRAWING FIGURES
[0007] For a better understanding of the present invention, and to show more clearly how it may be carried into effect, reference will now be made, by way of example, to the accompanying drawings, which show a preferred embodiment of the present invention and in which:
[0008] Figure 1 is a schematic view of a known pressure control system;
[0009] Figure 2 is a schematic view of an embodiment of a pressure control system according to the present invention;
[0010] Figure 3 is an enlarged portion of the schematic view of Figure
2 showing a regulator in greater detail;
[0011] Figure 4 is an enlarged portion of the schematic view of Figure
2 showing a inspirator in greater detail;
[0012] Figure 5 is an enlarged portion of the schematic view of Figure
2 showing a primary pilot in greater detail;
[0013] Figure 6 is an enlarged portion of the schematic view of Figure
2 showing a secondary pilot in greater detail; [0014] Figure 7 shows an end view of a portion of the regulator of
Figure 2; and
[0015] Figure 8 shows test results of pressure at a fuel cell stack inlet with various process fluid flows using the pressure control system of Figure
2.
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENT [0100] A known pressure control system is shown generally at 10 in
Figure 1. The pressure control system 10 comprises an unloading type flexible element pressure regulator 20 and a piloting system. The pressure regulator 20 is disposed in the process fluid stream line 40 and in operation, allows the process fluid to flow through a chamber 24 thereof disposed on one side of the flexible element, e.g. a diaphragm 28. A divider 22 is disposed in the chamber 24 to adjust the pressure therein. The divider 22 initially abuts against the flexible element 28 and hence prevents the process fluid from flowing through the chamber 24. As the process fluid is continuously fed into the chamber 24, pressure in the chamber 24 increases and the diaphragm 28 is lifted. This permits the flow of the process fluid through the chamber 24. A pilot controller 30 senses, via a sense line 60, the pressure at the point 50 where the pressure of the process fluid stream is to be accurately controlled, and correspondingly controls, via a control line 80, the pressure of another chamber 26 on the other side of the flexible element 28 of the pressure regulator 20, thereby eventually balancing the pressure on both sides of the flexible element 28, at a desired pressure. A further line 32, including an orifice or throttle 34 is connected to the pilot controller 30, and an exhaust line 36 is also provided. By manually adjusting the preset pressure of the pilot controller 30, the pressure of the process fluid stream at the desired point 50 can be controlled. As mentioned above, this system needs a pressure differential across the pressure regulator 20 to activate. It is inadequate to achieve accurate pressure control in low- pressure conditions.
[0101] In use, fluid is supplied through the line 32 and orifice 34 to the pilot controller 30. When too low a pressure is sensed by the controller 30, it is maintained in a closed position, so that flow from the line 32 is directed to the line 80 to maintain the pressure regulator 20 closed, thereby to increase the pressure in the line 40. When sufficient pressure is present in the line 40, this pressure is applied through the sense line 60 to the pilot controller 30 to open the controller against the action of the spring indicated therein. This permits at least part of the flow from line 32 to be exhausted through the exhaust line 36 to the outlet of the pressure regulator 20. Consequently, the pressure on the diaphragm 28 is reduced, permitting the regulator 20 to open, thereby to reduce the pressure in the line 40.
[0102] A pressure control system according to the present invention is shown generally at 110 in Figure 2. The pressure control system 110 has a pressure regulator 112, an inspirator 114, a primary (low pressure) pilot 116, and a secondary (higher pressure) pilot 118.
[0103] The pressure regulator 112 is mounted in a process fluid line
102 to adjustably control the rate of flow of a fluid through the line 102. More particularly, the regulator 112 has an inlet port 120a in fluid communication with an upstream line 102a of the process fluid line 102, and an outlet port 120b in fluid communication with a downstream line 102b of the process fluid line 102. As best seen in Figure 3, the regulator 112 is further provided with a flow channel 122 extending between the inlet and outlet ports 102a, 102b and with a closure means 124 in the flow channel 122. The closure means 124 is variably adjustable between a fully closed position, in which the ports 102a and 102b are fluidly isolated from each other, and a fully open position in which a maximum rate of flow is permitted through the flow channel 122.
[0104] In the embodiment illustrated, the closure means 124 comprises a sealing surface 126 attached to a flexible actuating diaphragm 128. The diaphragm 128 serves as an actuator for advancing the sealing surface 126 towards, or retracting the sealing surface 126 away from, an engagement surface 130 provided on a divider element 132. The divider element 132 can be in the form of a fixed wall extending into the flow channel 122. When the sealing surface 126 abuts the engagement surface 130, the closure means 124 is in the fully closed position and flow through the channel 122 is denied.
[0105] The actuating diaphragm 128 can move in response to a pressure differential across the thickness of the diaphragm 128. Accordingly, in the embodiment illustrated, one face 129a of the diaphragm 128 (i.e. the face with the sealing surface 126) partially defines the flow channel 122, and the opposite face 129b of the diaphragm 128 partially defines a control chamber 136. By controlling pressure in the control chamber 136 relative to that of the flow channel 122, the position of the actuating diaphragm 128, and hence of the closure means 124, can be controlled, and moved between a fully lowered position 128a and a fully raised position 128b (shown in phantom in Figure 3), corresponding to fully closed and fully open positions of the valve closure means 124. In steady state operation, the pressures in the flow channel 122 and control chamber 136 are equal, and the diaphragm 128 is substantially stationary. [0106] According to the present invention, the pressure in the control chamber 136 is adjusted by forcing actuator fluid into, or evacuating actuator fluid from, the chamber 136 via a pressure control line 138 that extends between the chamber 136 and the inspirator 114 (Figure 2). More particularly, the inspirator 114 has, in the form of a venturi, a converging inlet 140, a diverging outlet 142, and a throat 144 between the inlet 140 and outlet 142. The pressure control line 138 extends between the control chamber 136 and the throat 144 of the inspirator 114 (Figure 4). [0107] The inspirator 114 receives a flow of actuator fluid at its inlet
140 via an inspirator supply line 146, and discharges a flow of actuator fluid from its outlet 142 via an inspirator vent line 148. According to one embodiment of the present invention, the fluid in the supply line 146 is supplied at a relatively constant, higher than target, pressure from a fluid source independent of the process fluid in line 102. The flow of fluid through the inspirator 114 is accelerated in the inspirator, so that a pressure drop is generated at the throat 144 of the inspirator. At a high rate of fluid flow across the inspirator 114 (e.g. unrestricted venting), the pressure drop can generate suction in the control chamber 136 to lift the diaphragm 128 and open the closure member 124. On the other hand, if the venting is restricted, fluid entering the inlet 140 can be directed into the chamber 136, thereby urging the diaphragm 128 downwards and closing the closure member 124.
[0108] With respect to the outlet 142 of the inspirator 114, the outlet
142 is connected to the inspirator vent line 148 to provide fluid communication with the primary (low pressure) pilot 116 for controlled venting of the outlet 142. More particularly, and as best seen in Figure 5, the primary pilot 116 has a control portion 150 and a valve portion 152, which are in fluid isolation from each other. The valve portion 152 has an inlet port 154, an outlet port 156, and a valve member 158 between the inlet port 154 and outlet port 156. The inspirator vent line 148 connects the outlet 142 of the inspirator 114 to the inlet port 154 of the primary pilot 116. The outlet port 156 is open to atmosphere.
[0109] The valve member 158 can move among a fully closed position, a fully open position, and various degrees of partially open positions. In this way, the valve member 158 controls the flow of fluid from the inlet port 154 to the outlet port 156, and hence, the valve portion 152 of the primary pilot 116 controls the flow of fluid from the outlet 142 of the inspirator 114 to atmosphere.
[0110] The control portion 150 of the primary pilot 116 adjusts the position of the valve member 158 of the primary pilot 116. The control portion 150 has a target pressure chamber 160 and a sensed pressure chamber 162 that are separated from each other by a primary pilot diaphragm 164. The primary pilot diaphragm 164 has a target pressure face 165a exposed to the target pressure chamber 160, and a sensed pressure face 165b exposed to the sensed pressure chamber 162. A pressure adjustment spring 163 is housed within the target pressure chamber and exerts a force against the target pressure face 165a of the diaphragm 164, as does any fluid pressure in the target pressure chamber 160. By changing the relative pressures in the target and sensed pressure chambers 160, 162, the diaphragm 164 is moved towards one of the chamber 160, 162 dependent on the pressure differential and the load set on the spring 163, which can be adjustable. The valve member 158 is connected to the diaphragm 164 by, for example, a shaft 166 and a lever 168 pivotally mounted as shown, so that movement of the diaphragm 164 adjusts the position of the valve member 158. More particularly, a downward movement of the diaphragm 164 (movement towards the sensed pressure chamber 162) closes the valve member 158, and upward movement of the diaphragm 164 (towards the target pressure chamber 160) opens the valve member 158. In the embodiment illustrated, the spring 163 is relatively soft and the surface area of the faces 165a and 165b of the diaphragm 164 are relatively large so that the diaphragm 164 has greater sensitivity to small pressure differentials across the diaphragm 164.
[0111] The target pressure chamber 160 of the primary pilot valve
116 is in fluid communication with a target (or control) pressure input 170. More particularly, the control input 170 (Figure 2) can be a pressurized supply of fluid regulated by, for example, but not limited to, an electronic pressure regulator, and connected to a target port 172 of the target pressure chamber 160 via a control line 174.
[0112] The sensed pressure chamber 162 of the primary pilot valve
116 is in fluid communication with a point 178 in the process fluid line 102 where the process pressure is to be controlled. In the embodiment illustrated, the point 178 where the system pressure is to be controlled is located in the upstream line 102a of the process fluid line 102. In other embodiments, the point 178 can be located in other positions of the system, such as, for example, but not limited to, the downstream line 102b of the process fluid line 102. A sense line 180 extends from a sense port 182 of the sensed pressure chamber 162 to an orifice in the line 102 at the point 178. In this way, the pressure of the fluid stream in the line 102 at the point 178 is reflected by the pressure in the sensed pressure chamber 162. [0113] In operation, a pressure drop in the sensed system pressure
(i.e. in pressure chamber 162) may be caused by an increase in fluid flow through the regulator 112 (i.e. an increase in fluid consumption by the system). The higher pressure in the target pressure chamber 160 of the pilot 116 presses the diaphragm 164 towards the sensed pressure chamber 162, which therefore moves the valve member 158 to a more closed position. This restricts the flow of fluid from the outlet 142 of the inspirator 114 to the atmosphere, which in turn increases the pressure in the pressure control line 138 and in the pressure control chamber 136. As a result, the actuator diaphragm 128 advances towards the engagement surface 130 of the divider 132, thereby restricting flow through the flow channel 122 of the regulator 112 and increasing the pressure at the sensing point 178. [0114] An increase in the sensed system pressure (at point 178, and in the sensed pressure chamber 162) may be caused by a decrease in fluid flow through the regulator 112 (i.e. a decrease in fluid consumption by the system). The higher pressure in the sensed pressure chamber 162 pushes the pilot diaphragm 164 towards the target pressure chamber 160, so that the valve member 158 is moved to a more open position. This increases the flow of fluid from the outlet 142 of the inspirator 114, which in turn reduces the pressure in the pressure control line 138 and the pressure control chamber 136 of the regulator 112. As a result, the diaphragm 128 retracts away from the engagement surface 130 of the divider 132, which increases flow through the channel 122 and decreases the pressure at the sensing point 178.
[0115] Accordingly, in response to a sensed pressure that is either higher or lower than the target pressure, the pressure control system 110 reacts to counteract the pressure deviation.
[0116] Further details of the fluid supply to the inlet 140 of the inspirator 114 will now be provided. A supply of actuator fluid through the inspirator supply line 146 can be provided by an independent (or auxiliary) fluid supply 188 that is passed through the secondary (higher pressure) pilot 118. The actuator fluid supply 188 can be a supply of any fluid that is isolated from the process fluid line 102, and is preferably supplied at a pressure greater than the target pressure input 170. [0117] As best seen in Figure 6, the secondary pilot 118 has a control portion 190 and a valve portion 192, which are fluidly isolated from each other. The valve portion 192 has an inlet port 194 and an outlet port 196, and a valve member 198 between the inlet port 194 and outlet port 196. An auxiliary supply line 199 connects the auxiliary fluid supply 188 to the inlet port 194 of the auxiliary pilot 118. The outlet port 196 is connected to the inspirator supply line 146.
[0118] The valve member 198 can move among a fully closed position, a fully open position, and various degrees of partially open positions, so that the valve portion 192 of the secondary pilot 118 controls the flow of fluid from the auxiliary fluid supply 188 to the inlet 140 of the inspirator 114.
[0119] The control portion 190 of the secondary pilot 118 adjusts the position of the valve member 198 of the secondary pilot 118. The control portion 190 has a target pressure chamber 200 and a sensed pressure chamber 202 that are separated from each other by a secondary pilot diaphragm 204. The secondary pilot diaphragm 204 has a target pressure face 205a exposed to the target pressure chamber 200, and a sensed pressure face 205b exposed to the sensed pressure chamber 202. A pressure adjustment spring 203 is housed within the target pressure chamber 200 and exerts a force against the target pressure face 205a of the diaphragm 204, as does any fluid pressure in the target pressure chamber 200. The force of the spring 203 can be adjusted by turning an adjustment screw 207 to change the preload on the spring 203. By changing the relative pressures in the target and sensed pressure chambers 200, 202, the diaphragm 204 is moved towards the chamber 200, 202 with the reduced pressure. The valve member 198 can be connected to the diaphragm 204 by, for example, a shaft 206, so that movement of the diaphragm 204 adjusts the portion of the valve member 198. In the embodiment illustrated, the spring 203 is relatively stiff and the surface area of the faces 205a and 205b of the diaphragm 204 are relatively small (compared to those of the primary pilot 116).
[0120] The target pressure chamber 200 of the secondary pilot valve
118 can be in fluid communication with the control pressure input 170. More specifically, the control (or target) pressure input 170 can be in communication with the chamber 200 via a secondary pilot control line 210 connecting the control line 174 of the primary pilot 116 to a target port 212 of the chamber 200. A stabilizing needle valve 213 can be provided in the secondary pilot control line.
[0121] The outlet port 196 of the secondary pilot valve 118 is in fluid communication with the inspirator supply line 146. A sense line 214 extends from a sense port 216 of the sensed pressure chamber 202 to an orifice in the inspirator supply line 146 between the outlet port 196 of the valve portion 192 of the secondary pilot 118 and the inlet 140 of the inspirator 114. [0122] In operation, the auxiliary fluid supply 188 can be supplied to the pressure control system 110, via the line 199, at a pressure that is greater than the target pressure (which is set as desired by the target pressure input 170). Without any additional force exerted on the diaphragm 204 by the spring 203, the fluid pressure to the outlet 196 of the secondary pilot 118 (and hence, the fluid pressure to the inlet 140 of the inspirator 114) is generally equal to the system target pressure. By adjusting the screw 207 to increase the force on the target face 205a of the diaphragm 204, fluid at a higher pressure can be passed to the inspirator. Accordingly, a greater pressure difference can be generated across the diaphragm 128 of the regulator 112.
[0123] Referring again to Figure 1, in known pressure control systems using regulators 20, the regulator 20 is usually positioned so that the diaphragm 28 is facing vertically upwards, or in other words, the diaphragm 28 is generally horizontal having the chamber 26 above and the chamber 24 below. The divider 22 is oriented generally vertically, and a partial gap or flow channel is provided between the top of divider 22 and the bottom of diaphragm 28. The inventors have observed that when a process fluid stream comprises a saturated gas stream, a problem can occur if liquid is condensed in the chamber 24 of the pressure regulator 20. As the gas stream flows through the chamber 24, liquid can condense and accumulate in the upstream side (left side in Figure 1) of the divider 22 causing partial blockage of the flow passage which can in turn create a significant pressure change in the gas stream. This can result in instability of pressure control and is therefore undesirable.
[0124] To overcome this problem, the pressure regulator 112 of the control system 110 can be rotated approximately 90 degrees around its axial direction, i.e. the direction of the process fluid stream therethrough (Figure 7). As a result, during operation, the divider 132 is disposed generally in horizontal position, and the diaphragm 128 extends in a generally vertical direction, with the flow channel 122 on one side and the chamber 136 on the other side. In this configuration, condensed liquid can more easily flow through the flow channel 122 between the surfaces 126 and 130. This can eliminate any significant pressure change due to condensation, so that the pressure of the process gas stream can be controlled constantly at a steady level.
[0125] In one application of the pressure control system 110, a fuel cell stack was placed between the pressure control point 178 in the line 102a and the inlet 120a of the pressure regulator. Test results of this example are provided hereinafter. It is to be appreciated, however, that the present system 110 can be used to control pressure of the process fluid stream at any arbitrary location along the process fluid stream line. It is also to be appreciated that the present invention can be applied in many industrial applications, where accurate control of the pressure of a process fluid stream is desirable, especially under low pressure conditions, including but not limited to a fuel cell system.
EXAMPLE
[0126] In a test run, the control pressure at inlet 170 was set at about
20psi. The auxiliary supply stream was provided at about 100psi. The adjustment screw 207 was adjusted so that the total force exerted on the target pressure face 205a of the diaphragm 204 was equivalent to about 25psi. A fluid consuming device in the form of a load cell stack was disposed in the upstream fluid line 102a, between the control point and the regulator 112.
[0127] Figure 4 shows test results when the present pressure control system in employed in a fuel cell system. As can be seen, although the process gas flow changes dramatically from near zero slpm to 200 slpm, the pressure of the process fluid at a certain point in the system is maintained at reasonably constant level.
[0128] The invention has been described in relation to a configuration where the pressure is sensed upstream from the pressure regulator 112. In particular, the invention is intended for particular application with fluid cell stacks where the fluid cell stacks are interposed between the sensing port 178 and the pressure regulator 112. However, the invention also has applicability where it is desired to control the pressure downstream from the pressure regulator 112. In this case, the operation of the first pilot valve 116 will need to be reversed. Thus, if the downstream pressure was sensed to be too high then it would be necessary to reduce the flow of fluid through the pressure regulator 112 to the downstream location. In response to excess sensed pressure, the valve member 158 would need to moved to a more closed position thereby to reduce the flow from the inspirator 114, in turn increasing the pressure of the actuating fluid delivered through the line 138 to the pressure regulator 112, so as to tend to close the pressure regulator 112 and reduce flow of fluid through it. Correspondingly, if the downstream pressure is sensed to be too low, then the pilot valve 116 needs to be opened so as to permit greater flow of fluid through it from the inlet port 154 to the outlet port 156. This greater flow of actuating fluid would reduce the pressure at the throat of the inspirator 114, in turn reducing the pressure applied to the pressure regulator 112, so as to let greater flow of fluid through the pressurized regulator 112, so as in turn to increase the downstream pressure.
[0129] While the above description constitutes the preferred embodiments, it will be appreciated that the present invention is susceptible to modification and change without departing from the fair meaning of the proper scope of the accompanying claims.

Claims

WE CLAIM:
1. A pressure control system for controlling the pressure of a process fluid stream at a certain location, the pressure control system comprising: a. a pressure regulator including an actuating element actuated by pressure of an actuating fluid to control opening of the pressure regulator; b. a fluid control means, contected to the pressure regulator, to control supply of the actuating fluid to the pressure regulator and thereby to control the pressure regulator; c. a first pilot valve, including a sense port for a sensed fluid pressure at a predetermined location, an inlet port connected to the fluid control means and a first valve actuatable in response to the sensed fluid pressure to control flow of the actuating fluid from the fluid control means and thereby to control flow of the actuating fluid to the pressure regulator; d. a second pilot valve, including an inlet port for an auxiliary fluid, an input for setting a desired fluid pressure, an outlet port for the auxiliary fluid conected to the fluid control means, and a second valve actuable to deliver the auxiliary fluid at the desired auxiliary fluid pressure to the fluid control means.
2. A pressure control systems claimed in claim 1 , wherein the fluid control means comprises an inspirator having an inlet, an outlet and throat between the inlet and the outlet thereof, wherein the pressure regulator includes a control chamber partially defined by the actuating element and connected to the throat of the inspirator, the outlet port of the second pilot valve is connected to the inlet of the inspirator and the outlet of the inspirator is connected to the inlet port of the first pilot valve for the actuating fluid, whereby, in use, with the first valve substantially open, actuating fluid can flow through the inspirator from the inlet to the outlet thereof, to created a low pressure in the throat and in the control chamber of the pressure regulator, and with the first valve substantially closed, flow of the actuating fluid from the outlet of the inspirator is substantially prevented, thereby to increase the pressure of the throat and in the control chamber of the pressure regulator.
3. A pressure conrtol control system as claimed in claim 1 or 2, wherein the first pilot valve includes a target pressure chamber and a sensed pressure chamber, the target pressure chamber including a first target port for inputing a target pressure, and the sensed pressure chamber including the sense port, and a first diaphragm means subject to the pressures of the target pressure and sensed pressure chambers and connected to the first valve for actuation thereof.
4. A pressure conrtol control system as claimed in claim 3, wherein the first valve of the first pilot valve includes an outlet port open to atmosphere, whereby when the first valve is open, the inlet port for the actuating fluid is connected to atmosphere.
5. A pressure conrtol control system as claimed in claim 4, wherein the first pilot valve includes means for adjusting the pressure differential between the pressures in the sensed and target pressure chambers necessary to open the first valve of the first pilot valve.
6. A pressure conrtol control system as claimed in claim 5, wherein the first valve of the first pilot valve includes a shaft, and wherein the pilot valve includes a lever pivotably connected to said shaft, to a housing of the first pilot valve and to the first diaphragm means, for actuation of the first valve.
7. A pressure conrtol control system as claimed in any one of claims 1- 6, wherein the second pilot valve includes a second target pressure chamber and a second sensed pressure chamber.and a second target port for a target fluid pressure, wherein the outlet port for the auxiliary fluid is connected to the second sensed pressure chamber, wherein a second diaphragm is provided between the second target and second sensed pressure chambers and is connected to the second valve to control actuation thereof.
8. A pressure control system as claimed in claim 7, wherein the second pilot valve includes means for varying a target pressure differential between the second target and second sensed pressure chambers necessary to displace the second diaphragm and thereby displace the second valve, to control flow of the auxiliary gas from the inlet port for the auxiliary fluid to the outlet port for the auxiliary fluid.
9. A pressure control system as claimed in claim 7 or 8 which includes a common input port for a target pressure signal, connected to the first and second target ports.
10. A pressure control system as claimed in claim 9, including a stablizing needle valve provided between the common input port and and the second target port.
11. A pressure control system as claimed in any preceeding claim, wherein the pressure regulator comprises a flexible actuating diaphragm incorporating the actuating element and a sealing surface, whereby sufficient pressure of the actuating fluid presses the pressure regulator diaphragm against the sealing surface to close the pressure regulator.
12. A pressure control system as claimed in claim 11 , wherein the pressure regulator is mounted with the diaphragm and the sealing surface extending substantially vertically.
13. A pressure control system as claimed in any preceeding claim, wherein the sense port of the first pilot valve is adapted for connection to the process fluid line upstream of the pressure regulator, and wherein the first pilot valve is adapted to open the first valve thereof in response to eccess sensed fluid pressure, thereby to permit actuating fluid to flow from the fluid control means, reduce pressure of the actuating fluid in the pressure regulator and thereby to open the pressure regulator, to reduce the fluid pressure upstream thereof, and correspondingly, in respose to a sensed fluid pressure that is too low, to close the first valve, to reduce flow of actuating fluid from the fluid control means, and thereby to increase the pressure of the actuating fuild in the presure regulator, to close the pressure regulator and to increase the fluid pressure upstream from the pressure regulator.
14. A pressure control system as claimed in anyone of claims 1 to 12, wherein the sense port of the first pilot valve is adapted for connection to the preocess fluid line downstream from the pressure regulator, wherein the first pilot valve is adapted, in response to excess sensed fluid pressure, to close the first valve thereof, to reduce the flow of actuating fluid from the fluid control means, to increase the pressure of the actuating fluid in the pressure regulator, and thereby to close the pressure regulator to decease fluid pressure downstream therefrom, and correspondingly, in response to a sensed fluid pressure that is too low, to open the first valve, to vent the actuating fluid from the fluid control means, to reduce the pressure of the actuating fluid in the pressure regualator and thereby to open the pressure regulator to increase the fluid pressure downstream therefrom.
PCT/CA2003/001787 2002-11-20 2003-11-20 Inspirated pressure control system WO2004046841A1 (en)

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Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2006084834A1 (en) * 2005-02-11 2006-08-17 Robert Bosch Gmbh Fuel cell installation comprising a metering unit
WO2006084886A1 (en) * 2005-02-11 2006-08-17 Robert Bosch Gmbh Fuel cell system comprising a metering unit
AU2005271274B2 (en) * 2004-08-04 2010-03-04 Shire Holdings Ag Quinazoline derivatives and their use in the treatment of thrombocythemia
DE102012219061A1 (en) * 2012-10-19 2014-04-24 Robert Bosch Gmbh System for performing hydrogen supply of polymer electrolyte membrane fuel cell mounted in motor car, has pressure reducer with spring chamber that is pressure-loaded and spring-loaded by using prevailing pressure of valve piston
CN113015946A (en) * 2018-10-05 2021-06-22 艾默生过程管理调节技术公司 Control line stabilizer for pressure regulator

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Publication number Priority date Publication date Assignee Title
FR1110070A (en) * 1953-10-15 1956-02-06 Kromschroeder Ag G pressure wave transmitter and pressure wave amplifier for gas distribution networks
EP1205993A1 (en) * 2000-11-07 2002-05-15 Sulzer Hexis AG Method for operating a fuel cell battery with a control arrangement
US6418956B1 (en) * 2000-11-15 2002-07-16 Plast-O-Matic Valves, Inc. Pressure controller

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR1110070A (en) * 1953-10-15 1956-02-06 Kromschroeder Ag G pressure wave transmitter and pressure wave amplifier for gas distribution networks
EP1205993A1 (en) * 2000-11-07 2002-05-15 Sulzer Hexis AG Method for operating a fuel cell battery with a control arrangement
US6418956B1 (en) * 2000-11-15 2002-07-16 Plast-O-Matic Valves, Inc. Pressure controller

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
AU2005271274B2 (en) * 2004-08-04 2010-03-04 Shire Holdings Ag Quinazoline derivatives and their use in the treatment of thrombocythemia
WO2006084834A1 (en) * 2005-02-11 2006-08-17 Robert Bosch Gmbh Fuel cell installation comprising a metering unit
WO2006084886A1 (en) * 2005-02-11 2006-08-17 Robert Bosch Gmbh Fuel cell system comprising a metering unit
DE102012219061A1 (en) * 2012-10-19 2014-04-24 Robert Bosch Gmbh System for performing hydrogen supply of polymer electrolyte membrane fuel cell mounted in motor car, has pressure reducer with spring chamber that is pressure-loaded and spring-loaded by using prevailing pressure of valve piston
CN113015946A (en) * 2018-10-05 2021-06-22 艾默生过程管理调节技术公司 Control line stabilizer for pressure regulator

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