EP2816233B1 - Pump device and pump system - Google Patents
Pump device and pump system Download PDFInfo
- Publication number
- EP2816233B1 EP2816233B1 EP12868917.1A EP12868917A EP2816233B1 EP 2816233 B1 EP2816233 B1 EP 2816233B1 EP 12868917 A EP12868917 A EP 12868917A EP 2816233 B1 EP2816233 B1 EP 2816233B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- pressure
- valve
- gas
- pump
- discharge
- Prior art date
- Legal status (The legal status 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 status listed.)
- Active
Links
- 238000000034 method Methods 0.000 claims description 33
- 230000008569 process Effects 0.000 claims description 33
- 238000005192 partition Methods 0.000 claims description 3
- 239000007789 gas Substances 0.000 description 130
- 230000007246 mechanism Effects 0.000 description 31
- 239000000872 buffer Substances 0.000 description 15
- 230000010349 pulsation Effects 0.000 description 10
- 239000002737 fuel gas Substances 0.000 description 9
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 description 7
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 6
- 238000010586 diagram Methods 0.000 description 5
- 230000000903 blocking effect Effects 0.000 description 4
- 230000006835 compression Effects 0.000 description 4
- 238000007906 compression Methods 0.000 description 4
- 229920001971 elastomer Polymers 0.000 description 4
- 229920000459 Nitrile rubber Polymers 0.000 description 3
- 230000009471 action Effects 0.000 description 3
- 230000008859 change Effects 0.000 description 3
- 239000000446 fuel Substances 0.000 description 3
- 239000001257 hydrogen Substances 0.000 description 3
- 229910052739 hydrogen Inorganic materials 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 239000001294 propane Substances 0.000 description 3
- 235000014676 Phragmites communis Nutrition 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 238000002485 combustion reaction Methods 0.000 description 2
- 238000002474 experimental method Methods 0.000 description 2
- 150000002431 hydrogen Chemical class 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- 230000004913 activation Effects 0.000 description 1
- 230000003139 buffering effect Effects 0.000 description 1
- 239000000498 cooling water Substances 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 229920001973 fluoroelastomer Polymers 0.000 description 1
- 239000002828 fuel tank Substances 0.000 description 1
- 239000010720 hydraulic oil Substances 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 230000002401 inhibitory effect Effects 0.000 description 1
- -1 nitrile rubber (NBR) Chemical compound 0.000 description 1
- 238000010248 power generation Methods 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 238000011144 upstream manufacturing Methods 0.000 description 1
Images
Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04B—POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS
- F04B43/00—Machines, pumps, or pumping installations having flexible working members
- F04B43/02—Machines, pumps, or pumping installations having flexible working members having plate-like flexible members, e.g. diaphragms
- F04B43/04—Pumps having electric drive
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04B—POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS
- F04B45/00—Pumps or pumping installations having flexible working members and specially adapted for elastic fluids
- F04B45/04—Pumps or pumping installations having flexible working members and specially adapted for elastic fluids having plate-like flexible members, e.g. diaphragms
- F04B45/047—Pumps having electric drive
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04B—POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS
- F04B49/00—Control, e.g. of pump delivery, or pump pressure of, or safety measures for, machines, pumps, or pumping installations, not otherwise provided for, or of interest apart from, groups F04B1/00 - F04B47/00
- F04B49/06—Control using electricity
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04B—POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS
- F04B53/00—Component parts, details or accessories not provided for in, or of interest apart from, groups F04B1/00 - F04B23/00 or F04B39/00 - F04B47/00
- F04B53/10—Valves; Arrangement of valves
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04B—POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS
- F04B53/00—Component parts, details or accessories not provided for in, or of interest apart from, groups F04B1/00 - F04B23/00 or F04B39/00 - F04B47/00
- F04B53/10—Valves; Arrangement of valves
- F04B53/1037—Flap valves
- F04B53/1047—Flap valves the valve being formed by one or more flexible elements
- F04B53/106—Flap valves the valve being formed by one or more flexible elements the valve being a membrane
- F04B53/1065—Flap valves the valve being formed by one or more flexible elements the valve being a membrane fixed at its centre
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04B—POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS
- F04B2205/00—Fluid parameters
- F04B2205/03—Pressure in the compression chamber
Definitions
- the present invention relates to a pump device used as a booster blower or a booster pump, for example, and to a pump system equipped with the pump device.
- a pump device called booster blower or booster pump is widely known as a device that increases the pressure of gas such as a fuel gas and oxygen, liquid such as cooling water and hydraulic oil, and the like to a predetermined pressure.
- a roots pump, a diaphragm pump, and the like are used.
- Patent Document 1 below describes a diaphragm pump that is used as a booster blower for fuel gas in a fuel cell system.
- Patent Document 2 below refers to a high volumetric efficiency compression machine that can be used as a compressor, pump, or actuator, with a compression chamber being formed by a movable body and the inner wall of a casing. A discharge valve is formed in the casing, and communicates with the compression chamber.
- Patent Document 3 refers to a diaphragm pump for liquids.
- a conventional booster blower does not have a function of discharging an introduced gas at a reduced pressure. For that reason, in a pump system in which a pressure source that supplies a gas of a predetermined pressure or higher is connected to a suction port of the booster blower, the gas introduced to the suction port when the operation of the booster blower is stopped is discharged from the booster blower, and depending on circumstances, there arises a possibility of causing a problem with a system.
- a pump device including a casing, a movable member, a first valve, a second valve, and a third valve.
- the casing includes a suction port, a discharge port, and a pump chamber that can communicate with the suction port and the discharge port.
- the movable member is movable within the casing and alternately performs suction of a gas into the pump chamber and discharge of the gas from the pump chamber.
- the first valve is attached between the suction port and the pump chamber and permits the gas to flow from the suction port to the pump chamber.
- the second valve is attached between the pump chamber and the discharge port and permits the gas to flow from the pump chamber to the discharge port in a case where the gas of the pump chamber has a first pressure or higher.
- the third valve is attached to the discharge port and limits a flow of the gas toward the discharge port from the suction port in a case where the gas between the suction port and the discharge port has a second pressure or lower, the second pressure being higher than the first pressure.
- a pump system including a pump device, a pressure source, and a process unit.
- the pump device includes a casing, a movable member, a first valve, a second valve, and a third valve.
- the casing includes a suction port that communicates with the pressure source, a discharge port that communicates with the process unit, and a pump chamber that can communicate with the suction port and the discharge port.
- the movable member is movable within the casing and alternately performs suction of a gas into the pump chamber and discharge of the gas from the pump chamber.
- the first valve is attached between the suction port and the pump chamber and permits the gas to flow toward the pump chamber from the suction port.
- the second valve is attached between the pump chamber and the discharge port and permits the gas having a first pressure or higher to flow toward the discharge port from the pump chamber.
- the third valve is attached to the discharge port and limits a flow of the gas having a second pressure or lower to flow toward the discharge port from the suction port, the second pressure being higher than the first pressure.
- the pressure source is connected to the suction port and supplies the gas having the second pressure or lower to the pump device.
- the process unit is connected to the discharge port and processes the gas discharged from the pump device.
- a pump device including a casing, a movable member, a first valve, a second valve, and a third valve.
- the casing includes a suction port, a discharge port, and a pump chamber that can communicate with the suction port and the discharge port.
- the movable member is movable within the casing and alternately performs suction of a gas into the pump chamber and discharge of the gas from the pump chamber.
- the first valve is attached between the suction port and the pump chamber and permits the gas to flow from the suction port to the pump chamber.
- the second valve is attached between the pump chamber and the discharge port and permits the gas to flow from the pump chamber to the discharge port in a case where the gas of the pump chamber has a first pressure or higher.
- the third valve is attached to the casing and limits a flow of the gas toward the discharge port from the suction port in a case where the gas between the suction port and the discharge port has a second pressure or lower, the second pressure being higher than the first pressure.
- the movable member periodically changes the volume of the pump chamber, and thus alternately performs the suction of the gas into the pump chamber and the discharge of the gas from the pump chamber.
- the gas is suctioned
- the gas is introduced from the suction port to the pump chamber via the first valve.
- the gas introduced into the pump chamber is compressed to have a first pressure or higher by the movable member in the pump chamber, and thus the second valve is opened and the gas is discharged from the discharge port.
- the gas is discharged from the discharge port at a pressure equal to or higher than the first pressure.
- the second valve is opened at the time a pressure within the pump chamber reaches the first pressure or higher, and permits the gas to flow from the pump chamber to the discharge port. So, for example, when the gas is introduced at a pressure equal to or higher than the first pressure from the suction port to the pump chamber at the time the operation of the pump device is stopped, the flow of the gas that opens the second valve and flows toward the discharge port is formed.
- the pump device includes a third valve.
- the third valve limits the flow of the gas having the second pressure or lower, the second pressure being higher than the first pressure. So, even in the case where the gas having a pressure equal to or higher than the first pressure and equal to or lower than the second pressure is introduced from the suction port to the pump chamber at the time the operation of the pump device is stopped, the gas is inhibited from flowing by the third valve and the discharge of the gas from the discharge port is suppressed. With this, an unconsidered discharge of the gas at the time the operation is stopped is suppressed.
- the pump device since an unconsidered discharge of the gas at the time the operation of the pump device is stopped can be suppressed, the pump device can also be applied to a pump system in which a gas pressure source is connected to the suction port. With this, it is possible to eliminate a possibility of causing a problem with a system due to the leakage of the gas from the discharge port at the time the operation is stopped.
- the second pressure can be set as appropriate and is set based on the pressure of the gas introduced into the suction port or an allowable flow rate of the gas discharged in a state where the operation is stopped, for example.
- the phrase “limit the flow” contains the meaning of “block the flow” and the meaning of “reduce the flow rate without blocking the flow”.
- the third valve is attached to the discharge port.
- the third valve may have the structure capable of completely blocking the flow of the gas having the second pressure or lower or may have the structure in which the degree of opening changes in a stepwise manner between the first pressure and the second pressure.
- the third valve can be constituted of a solenoid valve, for example.
- the third valve includes a valve seat and a valve member that is capable of being seated on the valve seat and continuously changes the degree of opening in accordance with a pressure equal to or higher than the first pressure and equal to or lower than the second pressure.
- a valve having such a valve structure for example, an umbrella valve is applicable. With this, it is possible to control the gas discharged from the pump device at a low flow rate.
- the casing may further include a space portion obtained by expanding a part of a flow path that communicates between the second valve and the third valve.
- the space portion functions as a buffer space that buffers pulsations of a discharged gas. With this, it is possible to reduce the pulsations of the gas and discharge the gas at a stable flow rate. Further, in the case where the drive of the pump device is controlled based on a discharge flow rate, it is possible to perform stable drive control of the pump device.
- the pump device can be constituted of a diaphragm pump.
- the movable member includes a diaphragm that is deformable and partitions the pump chamber. With this, it is possible to provide a small pump device.
- a pump system including a pump device, a pressure source, and a process unit.
- the pump device includes a casing, a movable member, a first valve, a second valve, and a third valve.
- the casing includes a suction port that communicates with the pressure source, a discharge port that communicates with the process unit, and a pump chamber that can communicate with the suction port and the discharge port.
- the movable member is movable within the casing and alternately performs suction of a gas into the pump chamber and discharge of the gas from the pump chamber.
- the first valve is attached between the suction port and the pump chamber and permits the gas to flow toward the pump chamber from the suction port.
- the second valve is attached between the pump chamber and the discharge port and permits the gas having a first pressure or higher to flow toward the discharge port from the pump chamber.
- the third valve is attached to the casing and limits a flow of the gas having a second pressure or lower to flow toward the discharge port from the suction port, the second pressure being higher than the first pressure.
- the pressure source is connected to the suction port and supplies the gas having the second pressure or lower to the pump device.
- the process unit is connected to the discharge port and processes the gas discharged from the pump device.
- the pump system even in the case where the gas having a pressure equal to or higher than the first pressure and equal to or lower than the second pressure is introduced from the pressure source to the pump chamber at the time the operation of the pump device is stopped, the gas is inhibited from flowing by the third valve and the discharge of the gas from the discharge port is limited. With this, an unconsidered discharge of the gas at the time the operation is stopped is suppressed. Further, it is possible to eliminate a possibility of causing a problem with a system due to the leakage of the gas from the discharge port at the time the operation is stopped.
- the process unit is not particularly limited and includes various devices for generating energy and power by using the gas discharged from the pump device, such as a reformer, a combustor, a power generator, a cylinder device, and various engines.
- FIG. 1 is a diagram showing the outline of a pump system according to an embodiment of the present invention.
- a pump system 1 of this embodiment includes a pressure source 2, a pump device 3, a process unit 4, and a control unit 5.
- the pressure source 2 is connected to a suction side (primary side) of the pump device 3, and the process unit 4 is connected to a discharge side (secondary side) of the pump device 3.
- the pressure source 2 may be a container such as a tank and a cylinder to contain a gas of a predetermined pressure or may be a pressure generation source such as a compressor.
- the pump device 3 functions as a booster blower or a booster pump that increases a pressure PI of the gas, which is introduced from the pressure source 2, to a predetermined pressure P2 and supplies the gas to the process unit 4.
- the process unit 4 processes the gas supplied from the pump device 3 and generates energy, power, and the like.
- the control unit 5 controls the operation of the pump device 3, but may control the whole system including the process unit 4.
- the pump system 1 is applied to a fuel cell system, for example.
- the pressure source 2 corresponds to a fuel tank
- the pump device 3 boosts fuel gas (for example, city gas (methane) or LPG (liquefied propane gas)) and supplies the fuel gas to the process unit 4.
- the process unit 4 includes a reformer that transforms the fuel gas into hydrogen, a fuel cell that accumulates hydrogen, a power generation unit that causes hydrogen to react with oxygen, and the like.
- Fig. 2 is a cross-sectional view showing the configuration of the pump device 3.
- the pump device 3 is constituted of a diaphragm pump.
- the pump device 3 includes a metallic casing 10 and a drive unit 20.
- the casing 10 includes a pump body 11, a pump head 12, and a pump head cover 13.
- the drive unit 20 includes a motor 21 and a motor case 22.
- the pump body 11 forms an operating space 105 inside the casing 10, the operating space 105 containing a movable member 30.
- the movable member 30 includes a diaphragm 31, a fixture 32 that is fixed to the diaphragm 31, and a connecting rod 33 that couples the fixture 32 to the motor 21.
- the diaphragm 31 is formed of a disk-shaped rubber material, and its outer edge is sandwiched between the pump body 11 and the pump head 12.
- the fixture 32 is fixed to the center portion of the diaphragm 31 and is constituted of a plurality of components that are assembled so as to sandwich the diaphragm 31 in upward and downward direction.
- the connecting rod 33 is integrated with the fixture 32 so as to penetrate the center portion of the diaphragm 31.
- the connecting rod 33 is coupled to the periphery of an eccentric cam 35 via a bearing 34, the eccentric cam 35 being attached to a rotary shaft 210 of the motor 21.
- the pump head 12 includes a suction port 101 and a discharge port 102 and is disposed on the upper surface of an annular seating 110.
- the seating 110 is attached to an opening end of an upper portion of the pump body 11 and sandwiches the outer edge of the diaphragm 31 together with the pump head 12.
- the pump head 12 forms a pump chamber 100 together with the diaphragm 31.
- the pump head 12 includes a suction passage T1 that communicates between the suction port 101 and the pump chamber 100, and a discharge passage T2 that communicates between the pump chamber 100 and the discharge port 102.
- the pump chamber 100 is capable of communicating with the suction port 101 and the discharge port 102 via the suction passage T1 and the discharge passage T2, respectively.
- a suction valve 41 (first valve) and a discharge valve 42 (second valve) are attached to the suction passage T1 and the discharge passage T2, respectively.
- the suction valve 41 is attached to the pump head 12 so as to occlude a suction hole h1 that forms the suction passage T1.
- the suction valve 41 is constituted of a reed valve attached to an end of the suction hole h1 facing the pump chamber 100 and permits the gas to flow toward the pump chamber 100 from the suction port 101.
- the valve opening pressure of the suction valve 41 (minimum pressure required to open the suction valve 41) is not particularly limited and only needs to be a valve opening pressure enough to introduce gas of a predetermined flow rate (throughput) to the pump chamber 100 at the time the pump device is operated. So, the valve opening pressure of the suction valve 41 may be a pressure lower than the pressure of the gas supplied from the pressure source 2 to the pump device 3.
- the discharge valve 42 is attached to the pump head 12 so as to occlude a discharge hole h2 that forms the discharge passage T2.
- the discharge valve 42 is constituted of a reed valve attached to an end of the discharge hole h2 on the opposite side to the pump chamber 100 and permits the gas to flow toward the discharge port 102 from the pump chamber 100.
- the valve opening pressure of the discharge valve 42 (minimum pressure required to open the discharge valve 42) is, without being particularly limited, set to a pressure at which a target discharge pressure is obtained, and in this embodiment, set to a pressure (first pressure) higher than the valve opening pressure of the suction valve 41.
- the pump head cover 13 is attached to the upper portion of the pump head 12.
- Each of the suction passage T1 and the discharge passage T2 is formed by combination of the pump head 12 and the pump head cover 13.
- the pump body 11, the pump head 12, and the pump head cover 13 are integrally fixed using a plurality of screw members B.
- the motor 21 is constituted of a direct-current brushless motor capable of controlling the rotation speed and is contained in the cylindrical motor case 22.
- the motor 21 includes the rotary shaft 210, a stator 211, and a rotor 212.
- the stator 211 is fixed to an inner surface of the motor case 22, and the rotor 212 is fixed to a circumference of the rotary shaft 210.
- the rotary shaft 210 is supported by the motor case 22 via bearings 23 and 24, and a tip end of the rotary shaft 210 is attached to the rotation center of the eccentric cam 35.
- the eccentric cam 35 is formed such that its rotation center is eccentric relative to the inner race of the bearing 34. So, when the rotary shaft 210 rotates about its axis by the drive of the motor 21, the eccentric cam 35 rotates together with the rotary shaft 210, and thus the movable member 30 reciprocates vertically within the operating space 105. With this, the volume of the pump chamber 100 periodically changes and a predetermined pump function is obtained. The amount of reciprocation of the movable member 30 (stroke amount) is determined by an eccentricity amount of the eccentric cam 35.
- the pump device 3 further includes a valve mechanism 50 (third valve).
- the valve mechanism 50 is attached to the discharge port 102.
- the valve mechanism 50 has a function of limiting the outflow of gas from the discharge port 102 at the time the operation of the pump device 3 is stopped.
- Fig. 3 is a perspective cross-sectional view showing the configuration of the valve mechanism 50
- Fig. 4 is a cross-sectional view thereof.
- the valve mechanism 50 includes a valve member 51 made of rubber and a metallic housing 52 that contains the valve member 51.
- the housing 52 includes a first end 521 connected to the discharge port 102 of the casing 10 and a second end 522 connected to a pipe line (not shown) that communicates with the process unit 4.
- a seal ring 54 is fitted to the circumference of the first end 521, and the first end 521 is hermetically attached to the inside of the discharge port 102 by the seal ring 54.
- an inner passage 523 that communicates between the first end 521 and the second end 522 is formed inside the housing 52.
- a wall portion 53 including a plurality of holes 531 at its center portion and circumference is formed perpendicularly to a wall surface of the inner passage 523, and the first end 521 and the second end 522 are capable of communicating with each other via those holes 531.
- the valve member 51 is constituted of an umbrella valve. Specifically, the valve member 51 is formed into almost a disk shape and a shaft portion 511 formed at the center portion of the valve member 51 is fitted to a center hole of the wall portion 53. Thus, the valve member 51 is disposed in the inner passage 523. An outer edge 512 of the valve member 51 is elastically in contact with a valve seat 532 that is formed on a front surface of the wall portion 53 facing the second end 522, and stops the flow of the gas from the second end 522 side to the first end 521 side. Specifically, the valve member 51 functions as a backflow prevention valve.
- the valve member 51 permits the gas to flow in the forward direction from the first end 521 side to the second end 522 side by opening the valve at a predetermined pressure or higher.
- the valve member 51 moves away from the valve seat 532 because the outer edge 512 is elastically deformed to the second end 522 side, and a blocking state of the inner passage 523 by the valve member 51 is released.
- the outer edge 512 is seated on the valve seat 532, and the blocking state of the inner passage 523 is maintained.
- a rubber material having resistance to various process gases is used for the valve member 51.
- rubber materials having resistance to hydrocarbon gas including methane and propane such as nitrile rubber (NBR), hydrogenated nitrile rubber (HNBR), and fluoro-rubber (FKM), are used for the valve member 51.
- NBR nitrile rubber
- HNBR hydrogenated nitrile rubber
- FKM fluoro-rubber
- the thickness or size of the valve member 51 is not particularly limited and is set to a thickness or size enough to ensure a valve opening pressure compatible with various specifications.
- valve opening pressure of the valve member 51 (minimum pressure required to open the valve member 51) is set to a pressure that is at least higher than the valve opening pressure (first pressure) of the discharge valve 42.
- first pressure the valve opening pressure of the discharge valve 42.
- the valve member 51 limits the flow of gas having a predetermined pressure (second pressure) or lower, the predetermined pressure (second pressure) being higher than the valve opening pressure of the valve member 51.
- the valve opening pressure of the valve member 51 is determined by referring to the gas pressure PI supplied from the pressure source 2 of the pump system 1.
- the valve opening pressure of the valve member 51 is set to a pressure higher than the gas pressure PI of the pressure source 2. With this, even in the case where the gas pressure PI of the pressure source 2 is higher than the valve opening pressure of the discharge valve 42, it is possible to block the outflow of gas from the discharge port 102 to the process unit 4 when the operation of the pump device 3 is stopped and reliably prevent the outflow of gas to the process unit 4.
- valve opening pressure of the valve member may be set to a pressure lower than the gas pressure P2 of the pressure source 2.
- the pump device 3 is driven by activation of the motor 21 of the drive unit 20.
- the rotation speed of the motor 21 is controlled by the control unit 5 so as to obtain a constant discharge flow rate based on a flowmeter provided on the discharge side of the pump device 3, for example.
- the motor 21 reciprocates the movable member 30 in the operating space 105 with predetermined strokes by rotating the eccentric cam 35 via the rotary shaft 210. With this, the diaphragm 31 that partitions the pump chamber 100 moves up and down, and the volume of the pump chamber 100 changes periodically.
- the movable member 30 periodically changes the volume of the pump chamber 100 and thus alternately performs the suction of gas into the pump chamber 100 and the discharge of gas from the pump chamber 100.
- the fuel gas of the pressure PI for example, 2 kPa (gauge pressure)
- the fuel gas introduced into the pump chamber 100 is compressed by the movable member in the pump chamber 100 and is boosted.
- the discharge valve 42 and the valve mechanism 50 are opened.
- the fuel gas of the pressure P2 for example, 15 kPa (gauge pressure)
- the fuel gas of the pressure P2 for example, 15 kPa (gauge pressure)
- the discharge valve 42 is opened at the time when the pressure within the pump chamber 100 reaches the valve opening pressure of the discharge valve 42 or higher and permits the gas to flow from the pump chamber 100 to the discharge port 102. So, when the gas is introduced into the pump chamber 100 from the suction port 101 at a pressure equal to or higher than the valve opening pressure of the discharge valve 42 when the operation of the pump device 3 is stopped, the discharge valve 42 is opened and the flow of the gas toward the discharge port 102 is formed.
- the valve mechanism 50 is attached to the discharge port 102.
- the valve mechanism 50 has a valve opening pressure that is higher than the gas pressure (P1) of the pressure source 2. So, even in the case where the gas of the pressure PI is introduced from the suction port 101 to the pump chamber 100 when the operation of the pump device 3 is stopped, the flow of the gas is stopped by the valve mechanism 50 and the outflow of the gas from the discharge port 102 to the process unit 4 is prevented. In such a manner, since an unconsidered discharge of the gas when the operation is stopped is suppressed, it is possible to eliminate a possibility of causing a problem with a system.
- the valve mechanism 50 has the structure capable of continuously changing the degree of opening in accordance with an introduction pressure. With this, at the time the operation of the pump device 6 is restarted, the valve mechanism 50 can be opened in accordance with a discharge pressure, and gas of a necessary flow rate can be supplied to the process unit 4 rapidly.
- Fig. 5 shows a time change of the discharge flow rate of the pump device 3 when the operation and stop of the pump device 3 are repeated under experimental conditions shown in Fig. 6 .
- a is a buffer tank
- b is a pressure gauge
- c is suction piping
- d is a blower, which correspond to the pump device 3 of this embodiment.
- e is a pressure gauge
- f is discharge piping
- g is a fixed orifice
- h is a flowmeter.
- the minimum value of the discharge flow rate is zero and a function of confining gas by the valve mechanism 50 normally works when the operation of the pump device 3 is stopped. Further, it was also found that the discharge flow rate of the pump device 6 is stably maintained to have a constant value and reproducibility is high.
- Fig. 7 shows experimental results that indicate a change in discharge flow rate of the pump device 6 with respect to a rotation speed control voltage (Vsp) input to the motor 21 of the pump device 6.
- Vsp rotation speed control voltage
- Fig. 8 shows a pump device according to a second embodiment of the present invention.
- a configuration different from that of the first embodiment will be mainly described, and the configurations that are the same as those in the embodiment described above will be denoted by the same reference numerals and description thereof will be omitted or simplified.
- a pump device 6 of this embodiment is different from that of the first embodiment described above in the configuration of a valve mechanism 60 attached to the discharge port 102.
- the valve mechanism 60 includes a valve member 61 that configures an umbrella valve, and is provided in the inner passage of a housing 62 in the same form as in the first embodiment shown in Figs. 3 and 4 .
- the valve mechanism 60 of this embodiment has a function common to the first embodiment, the function of limiting the outflow of gas having the valve opening pressure (first pressure) or higher of the discharge valve 42 and the gas pressure PI (second pressure) or lower of the pressure source 2.
- the valve mechanism 60 of this embodiment is different from that of the first embodiment in that the valve mechanism 60 has a function of permitting gas to outflow from the discharge port 102 to the process unit 4 while suppressing the outflow to a predetermined amount or less when the operation of the pump device 6 is stopped.
- valve opening pressure of the valve member 61 of this embodiment is set to a pressure lower than the gas pressure PI of the pressure source 2. Since the valve mechanism 60 of the this embodiment has the structure capable of continuously changing the degree of opening in accordance with the gas pressure, the flow rate of gas outflowing to the process unit 4 side can be controlled in accordance with the pressure of gas introduced into the valve mechanism 60.
- a pressure required to fully open the valve member 61 is set to a pressure higher than the gas pressure P1 of the pressure source 2 (for example, equal to or lower than the discharge pressure (P2) at the time of normal operation of the pump device 3).
- the flow rate of gas having the valve opening pressure (first pressure) or higher of the discharge valve 42 and the gas pressure P1 (second pressure) or lower of the pressure source 2 can be controlled by the valve mechanism 60.
- the flow rate of gas supplied from the pressure source 2 can be adjusted to a predetermined flow rate to be supplied to the process unit 4.
- a throttle valve such as an orifice on an upstream or downstream side of the pump device 6, and this allows the number of components of the system to be reduced.
- This embodiment is suitably used for a system that needs to supply gas of a predetermined flow rate or lower to the process unit 4 also when the operation of the pump device 6 is stopped.
- Fig. 9 shows a pump device according to a third embodiment of the present invention.
- a configuration different from that of the first embodiment will be mainly described, and the configurations that are the same as those in the embodiments described above will be denoted by the same reference numerals and description thereof will be omitted or simplified.
- a pump device 7 of this embodiment includes a casing 70 including a pump body 11, a pump head 72, and a pump head cover 73.
- a suction port 101 and a discharge port 102 are formed in the pump head 72.
- the valve mechanism 50 described in the first embodiment is attached to the discharge port 102.
- a suction passage T1, a discharge passage T2, and a buffer tank 721 are formed in the pump head 72. At least a part of each of those passages is exposed to the outside from the upper surface of the pump head 72 and is covered with the pump head cover 73 via a seal member to be isolated from open air.
- a diaphragm pump structurally generates pulsations in discharge gas.
- the driving rotation speed of the pump is controlled based on a measured value of the flow rate of discharge gas
- a correct flow rate cannot be measured and the drive control of the pump becomes unstable.
- the discharge gas is fuel gas, there is a possibility that the pulsations cause unstable combustion or incomplete combustion.
- the pump device 7 of this embodiment includes the buffer tank 721 between the discharge passage T2 and the discharge port 102.
- the buffer tank 721 forms a space portion 74 between a discharge valve 42 (discharge passage T2) and the valve mechanism 50 by expanding a part of a flow path that communicates with the discharge valve 42 (discharge passage T2) and the valve mechanism 50.
- the buffer tank 721 has a function of buffering the pulsations of gas discharged from the discharge valve 42.
- the pump device 7 of this embodiment it is possible to reduce the pulsations of gas discharged from the valve mechanism 50 and discharge gas at a stable flow rate. Further, in the case where the drive of the pump device 7 is controlled based on the discharge flow rate, it is possible to perform stable drive control of the pump device 7. Further, since the pump and the buffer tank are integrated, it is not necessary to separately provide a buffer tank in the gas flow path of the pump system, and the system configuration can be simplified.
- the volume of the space portion 74 of the buffer tank 721 is determined based on the pulsations (pressure range) of the gas discharged from the discharge valve 42.
- Fig. 10 shows results of an experiment performed by the inventors of the present invention and shows a relationship between a buffer volume (cc) and a pressure range of gas discharged from the discharge port 102. As shown in Fig. 10 , as the volume of the space portion 74 becomes larger, the pressure range can be made smaller. For example, when the volume of the space portion 74 is set to 120 cc or more, the pulsation range can be reduced to 0.75 kPa or less.
- Fig. 10 shows a pump device according to a fourth embodiment of the present invention.
- a configuration different from that of the first embodiment will be mainly described, and the configurations that are the same as those in the embodiments described above will be denoted by the same reference numerals and description thereof will be omitted or simplified.
- a pump device 8 of this embodiment includes a casing 80, a drive unit 20, and a buffer tank 81.
- the casing 80 includes a suction port 101 and a discharge port 102, boosts gas suctioned from the suction port 101 in a pump chamber (not shown), and discharges the boosted gas from the discharge port 102 via the buffer tank 81.
- Fig. 11 is a cross-sectional view of the buffer tank 81 and the discharge port 102.
- a space portion 74 having a predetermined volume is formed within the buffer tank 81 and reduces pulsations of the discharge gas.
- the discharge port 102 communicates with the space portion 74, and a valve member 51 is attached to the inside of the discharge port 102.
- the valve member 51 has the same configuration as that of the first embodiment and has a function of limiting the outflow of gas having a predetermined pressure or less.
- valve member 51 as a valve mechanism is supported by the casing 80, the number of components can be reduced.
- Figs. 13 to 18 each show an outer appearance of the pump device 8.
- Fig. 13 is a front view
- Fig. 14 is a back view
- Fig. 15 is a plan view
- Fig. 16 is a bottom view
- Fig. 17 is a right side view
- Fig. 18 is a left side view.
- valve mechanism that limits the flow of the gas having a predetermined pressure or lower is attached to the discharge port, but the present invention is not limited thereto.
- the valve mechanism may be provided on a discharge passage between the discharge valve and the discharge port.
- valve member that constitutes the valve mechanism is not limited to the umbrella valve and may be constituted of a ball valve or a butterfly valve, for example.
- the pump device is constituted of the diaphragm pump, but the present invention is not limited thereto and can also be applied to another pump device such as a roots pump.
- the movable member that changes the volume of the pump chamber corresponds to rotors disposed to be opposed to each other.
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- Details Of Reciprocating Pumps (AREA)
Description
- The present invention relates to a pump device used as a booster blower or a booster pump, for example, and to a pump system equipped with the pump device.
- A pump device called booster blower or booster pump is widely known as a device that increases the pressure of gas such as a fuel gas and oxygen, liquid such as cooling water and hydraulic oil, and the like to a predetermined pressure. In this type of pump device, a roots pump, a diaphragm pump, and the like are used. For example,
Patent Document 1 below describes a diaphragm pump that is used as a booster blower for fuel gas in a fuel cell system.
Moreover,Patent Document 2 below refers to a high volumetric efficiency compression machine that can be used as a compressor, pump, or actuator, with a compression chamber being formed by a movable body and the inner wall of a casing. A discharge valve is formed in the casing, and communicates with the compression chamber. Two intake valves are formed in the casing, communicate with the compression chamber and are arranged symmetrically with respect to the axial direction of the discharge valve. A rod transmits reciprocation to the movable body.
Furthermore,Patent Document 3 below refers to a diaphragm pump for liquids. - Patent Document 1: Japanese Patent Application Laid-open No.
2009-47084 - Patent Document 2:
US Patent Application Laid-open No. 5,201,643 A ; - Patent Document 3: British Patent Application Laid-open No.
470 354 A - A conventional booster blower does not have a function of discharging an introduced gas at a reduced pressure. For that reason, in a pump system in which a pressure source that supplies a gas of a predetermined pressure or higher is connected to a suction port of the booster blower, the gas introduced to the suction port when the operation of the booster blower is stopped is discharged from the booster blower, and depending on circumstances, there arises a possibility of causing a problem with a system.
- In view of the circumstances as described above, it is an object of the present invention to provide a pump device and a pump system that are capable of limiting discharge of a gas when the operation is stopped.
- In order to achieve the object described above, according to an embodiment of the present invention, there is provided a pump device including a casing, a movable member, a first valve, a second valve, and a third valve.
- The casing includes a suction port, a discharge port, and a pump chamber that can communicate with the suction port and the discharge port.
- The movable member is movable within the casing and alternately performs suction of a gas into the pump chamber and discharge of the gas from the pump chamber.
- The first valve is attached between the suction port and the pump chamber and permits the gas to flow from the suction port to the pump chamber.
- The second valve is attached between the pump chamber and the discharge port and permits the gas to flow from the pump chamber to the discharge port in a case where the gas of the pump chamber has a first pressure or higher.
- The third valve is attached to the discharge port and limits a flow of the gas toward the discharge port from the suction port in a case where the gas between the suction port and the discharge port has a second pressure or lower, the second pressure being higher than the first pressure.
- Further, in order to achieve the object described above, according to an embodiment of the present invention, there is provided a pump system including a pump device, a pressure source, and a process unit.
- The pump device includes a casing, a movable member, a first valve, a second valve, and a third valve.
- The casing includes a suction port that communicates with the pressure source, a discharge port that communicates with the process unit, and a pump chamber that can communicate with the suction port and the discharge port.
- The movable member is movable within the casing and alternately performs suction of a gas into the pump chamber and discharge of the gas from the pump chamber.
- The first valve is attached between the suction port and the pump chamber and permits the gas to flow toward the pump chamber from the suction port.
- The second valve is attached between the pump chamber and the discharge port and permits the gas having a first pressure or higher to flow toward the discharge port from the pump chamber.
- The third valve is attached to the discharge port and limits a flow of the gas having a second pressure or lower to flow toward the discharge port from the suction port, the second pressure being higher than the first pressure.
- The pressure source is connected to the suction port and supplies the gas having the second pressure or lower to the pump device.
- The process unit is connected to the discharge port and processes the gas discharged from the pump device.
-
- [
Fig. 1] Fig. 1 is a diagram showing the outline of a pump system according to an embodiment of the present invention. - [
Fig. 2] Fig. 2 is a cross-sectional view of a pump device according to the embodiment of the present invention. - [
Fig. 3] Fig. 3 is a perspective cross-sectional view showing the configuration of a valve mechanism incorporated in the pump device. - [
Fig. 4] Fig. 4 is a cross-sectional view of the valve mechanism. - [
Fig. 5] Fig. 5 shows experimental results indicating a time change of a discharge flow rate of the pump device when the operation and stop of the pump device are repeated. - [
Fig. 6] Fig. 6 is a configuration diagram of piping used in the experiment shown inFig. 5 . - [
Fig. 7] Fig. 7 is a diagram for describing an action of the pump device. - [
Fig. 8] Fig. 8 is a cross-sectional view of a pump device according to a second embodiment of the present invention. - [
Fig. 9] Fig. 9 is a fragmentary exploded perspective view of a pump device according to a third embodiment of the present invention. - [
Fig. 10] Fig. 10 is a diagram for describing an action of the pump device shown inFig. 9 . - [
Fig. 11] Fig. 11 is a perspective view of a pump device according to a fourth embodiment of the present invention. - [
Fig. 12] Fig. 12 is a cross-sectional view of a main part of the pump device shown inFig. 11 . - [
Fig. 13] Fig. 13 is a front view of the pump device shown inFig. 11 . - [
Fig. 14] Fig. 14 is a back view of the pump device shown inFig. 11 . - [
Fig. 15] Fig. 15 is a plan view of the pump device shown inFig. 11 . - [
Fig. 16] Fig. 16 is a bottom view of the pump device shown inFig. 11 . - [
Fig. 17] Fig. 17 is a right side view of the pump device shown inFig. 11 . - [
Fig. 18] Fig. 18 is a left side view of the pump device shown inFig. 11 . - According to an embodiment of the present invention, there is provided a pump device including a casing, a movable member, a first valve, a second valve, and a third valve.
- The casing includes a suction port, a discharge port, and a pump chamber that can communicate with the suction port and the discharge port.
- The movable member is movable within the casing and alternately performs suction of a gas into the pump chamber and discharge of the gas from the pump chamber.
- The first valve is attached between the suction port and the pump chamber and permits the gas to flow from the suction port to the pump chamber.
- The second valve is attached between the pump chamber and the discharge port and permits the gas to flow from the pump chamber to the discharge port in a case where the gas of the pump chamber has a first pressure or higher.
- The third valve is attached to the casing and limits a flow of the gas toward the discharge port from the suction port in a case where the gas between the suction port and the discharge port has a second pressure or lower, the second pressure being higher than the first pressure.
- In the pump device, the movable member periodically changes the volume of the pump chamber, and thus alternately performs the suction of the gas into the pump chamber and the discharge of the gas from the pump chamber. When the gas is suctioned, the gas is introduced from the suction port to the pump chamber via the first valve. When the gas is discharged, the gas introduced into the pump chamber is compressed to have a first pressure or higher by the movable member in the pump chamber, and thus the second valve is opened and the gas is discharged from the discharge port. By repetition of the above operation, the gas is discharged from the discharge port at a pressure equal to or higher than the first pressure.
- The second valve is opened at the time a pressure within the pump chamber reaches the first pressure or higher, and permits the gas to flow from the pump chamber to the discharge port. So, for example, when the gas is introduced at a pressure equal to or higher than the first pressure from the suction port to the pump chamber at the time the operation of the pump device is stopped, the flow of the gas that opens the second valve and flows toward the discharge port is formed.
- In this regard, the pump device includes a third valve. The third valve limits the flow of the gas having the second pressure or lower, the second pressure being higher than the first pressure. So, even in the case where the gas having a pressure equal to or higher than the first pressure and equal to or lower than the second pressure is introduced from the suction port to the pump chamber at the time the operation of the pump device is stopped, the gas is inhibited from flowing by the third valve and the discharge of the gas from the discharge port is suppressed. With this, an unconsidered discharge of the gas at the time the operation is stopped is suppressed.
- Further, according to the pump device, since an unconsidered discharge of the gas at the time the operation of the pump device is stopped can be suppressed, the pump device can also be applied to a pump system in which a gas pressure source is connected to the suction port. With this, it is possible to eliminate a possibility of causing a problem with a system due to the leakage of the gas from the discharge port at the time the operation is stopped.
- The second pressure can be set as appropriate and is set based on the pressure of the gas introduced into the suction port or an allowable flow rate of the gas discharged in a state where the operation is stopped, for example. The phrase "limit the flow" contains the meaning of "block the flow" and the meaning of "reduce the flow rate without blocking the flow".
- The third valve is attached to the discharge port. With this, a stable pump performance can be ensured without inhibiting the gas introduced into the pump chamber from flowing.
- The third valve may have the structure capable of completely blocking the flow of the gas having the second pressure or lower or may have the structure in which the degree of opening changes in a stepwise manner between the first pressure and the second pressure. In the former case, the third valve can be constituted of a solenoid valve, for example.
- On the other hand, in the latter case, a valve structure in which the degree of opening increases in accordance with the pressure is adopted for the third valve. For example, the third valve includes a valve seat and a valve member that is capable of being seated on the valve seat and continuously changes the degree of opening in accordance with a pressure equal to or higher than the first pressure and equal to or lower than the second pressure. As a valve having such a valve structure, for example, an umbrella valve is applicable. With this, it is possible to control the gas discharged from the pump device at a low flow rate.
- The casing may further include a space portion obtained by expanding a part of a flow path that communicates between the second valve and the third valve. The space portion functions as a buffer space that buffers pulsations of a discharged gas. With this, it is possible to reduce the pulsations of the gas and discharge the gas at a stable flow rate. Further, in the case where the drive of the pump device is controlled based on a discharge flow rate, it is possible to perform stable drive control of the pump device.
- The pump device can be constituted of a diaphragm pump. In this case, the movable member includes a diaphragm that is deformable and partitions the pump chamber. With this, it is possible to provide a small pump device.
- According to an embodiment of the present invention, there is provided a pump system including a pump device, a pressure source, and a process unit.
- The pump device includes a casing, a movable member, a first valve, a second valve, and a third valve.
- The casing includes a suction port that communicates with the pressure source, a discharge port that communicates with the process unit, and a pump chamber that can communicate with the suction port and the discharge port.
- The movable member is movable within the casing and alternately performs suction of a gas into the pump chamber and discharge of the gas from the pump chamber.
- The first valve is attached between the suction port and the pump chamber and permits the gas to flow toward the pump chamber from the suction port.
- The second valve is attached between the pump chamber and the discharge port and permits the gas having a first pressure or higher to flow toward the discharge port from the pump chamber.
- The third valve is attached to the casing and limits a flow of the gas having a second pressure or lower to flow toward the discharge port from the suction port, the second pressure being higher than the first pressure.
- The pressure source is connected to the suction port and supplies the gas having the second pressure or lower to the pump device.
- The process unit is connected to the discharge port and processes the gas discharged from the pump device.
- According to the pump system, even in the case where the gas having a pressure equal to or higher than the first pressure and equal to or lower than the second pressure is introduced from the pressure source to the pump chamber at the time the operation of the pump device is stopped, the gas is inhibited from flowing by the third valve and the discharge of the gas from the discharge port is limited. With this, an unconsidered discharge of the gas at the time the operation is stopped is suppressed. Further, it is possible to eliminate a possibility of causing a problem with a system due to the leakage of the gas from the discharge port at the time the operation is stopped.
- The process unit is not particularly limited and includes various devices for generating energy and power by using the gas discharged from the pump device, such as a reformer, a combustor, a power generator, a cylinder device, and various engines.
- Hereinafter, embodiments of the present invention will be described with reference to the drawings.
-
Fig. 1 is a diagram showing the outline of a pump system according to an embodiment of the present invention. Apump system 1 of this embodiment includes apressure source 2, apump device 3, aprocess unit 4, and acontrol unit 5. - The
pressure source 2 is connected to a suction side (primary side) of thepump device 3, and theprocess unit 4 is connected to a discharge side (secondary side) of thepump device 3. Thepressure source 2 may be a container such as a tank and a cylinder to contain a gas of a predetermined pressure or may be a pressure generation source such as a compressor. Thepump device 3 functions as a booster blower or a booster pump that increases a pressure PI of the gas, which is introduced from thepressure source 2, to a predetermined pressure P2 and supplies the gas to theprocess unit 4. Theprocess unit 4 processes the gas supplied from thepump device 3 and generates energy, power, and the like. Thecontrol unit 5 controls the operation of thepump device 3, but may control the whole system including theprocess unit 4. - The
pump system 1 is applied to a fuel cell system, for example. In this case, thepressure source 2 corresponds to a fuel tank, and thepump device 3 boosts fuel gas (for example, city gas (methane) or LPG (liquefied propane gas)) and supplies the fuel gas to theprocess unit 4. Theprocess unit 4 includes a reformer that transforms the fuel gas into hydrogen, a fuel cell that accumulates hydrogen, a power generation unit that causes hydrogen to react with oxygen, and the like. - Next, the
pump device 3 will be descried in detail with reference toFig. 2. Fig. 2 is a cross-sectional view showing the configuration of thepump device 3. In this embodiment, thepump device 3 is constituted of a diaphragm pump. - The
pump device 3 includes ametallic casing 10 and adrive unit 20. Thecasing 10 includes apump body 11, apump head 12, and apump head cover 13. Thedrive unit 20 includes amotor 21 and amotor case 22. - The
pump body 11 forms anoperating space 105 inside thecasing 10, the operatingspace 105 containing amovable member 30. Themovable member 30 includes adiaphragm 31, afixture 32 that is fixed to thediaphragm 31, and a connectingrod 33 that couples thefixture 32 to themotor 21. - The
diaphragm 31 is formed of a disk-shaped rubber material, and its outer edge is sandwiched between thepump body 11 and thepump head 12. Thefixture 32 is fixed to the center portion of thediaphragm 31 and is constituted of a plurality of components that are assembled so as to sandwich thediaphragm 31 in upward and downward direction. The connectingrod 33 is integrated with thefixture 32 so as to penetrate the center portion of thediaphragm 31. The connectingrod 33 is coupled to the periphery of aneccentric cam 35 via abearing 34, theeccentric cam 35 being attached to arotary shaft 210 of themotor 21. - The
pump head 12 includes asuction port 101 and adischarge port 102 and is disposed on the upper surface of anannular seating 110. Theseating 110 is attached to an opening end of an upper portion of thepump body 11 and sandwiches the outer edge of thediaphragm 31 together with thepump head 12. Thepump head 12 forms apump chamber 100 together with thediaphragm 31. - The
pump head 12 includes a suction passage T1 that communicates between thesuction port 101 and thepump chamber 100, and a discharge passage T2 that communicates between thepump chamber 100 and thedischarge port 102. Thepump chamber 100 is capable of communicating with thesuction port 101 and thedischarge port 102 via the suction passage T1 and the discharge passage T2, respectively. A suction valve 41 (first valve) and a discharge valve 42 (second valve) are attached to the suction passage T1 and the discharge passage T2, respectively. - The
suction valve 41 is attached to thepump head 12 so as to occlude a suction hole h1 that forms the suction passage T1. Thesuction valve 41 is constituted of a reed valve attached to an end of the suction hole h1 facing thepump chamber 100 and permits the gas to flow toward thepump chamber 100 from thesuction port 101. The valve opening pressure of the suction valve 41 (minimum pressure required to open the suction valve 41) is not particularly limited and only needs to be a valve opening pressure enough to introduce gas of a predetermined flow rate (throughput) to thepump chamber 100 at the time the pump device is operated. So, the valve opening pressure of thesuction valve 41 may be a pressure lower than the pressure of the gas supplied from thepressure source 2 to thepump device 3. - On the other hand, the
discharge valve 42 is attached to thepump head 12 so as to occlude a discharge hole h2 that forms the discharge passage T2. Thedischarge valve 42 is constituted of a reed valve attached to an end of the discharge hole h2 on the opposite side to thepump chamber 100 and permits the gas to flow toward thedischarge port 102 from thepump chamber 100. The valve opening pressure of the discharge valve 42 (minimum pressure required to open the discharge valve 42) is, without being particularly limited, set to a pressure at which a target discharge pressure is obtained, and in this embodiment, set to a pressure (first pressure) higher than the valve opening pressure of thesuction valve 41. - The
pump head cover 13 is attached to the upper portion of thepump head 12. Each of the suction passage T1 and the discharge passage T2 is formed by combination of thepump head 12 and thepump head cover 13. Thepump body 11, thepump head 12, and thepump head cover 13 are integrally fixed using a plurality of screw members B. - The
motor 21 is constituted of a direct-current brushless motor capable of controlling the rotation speed and is contained in thecylindrical motor case 22. Themotor 21 includes therotary shaft 210, astator 211, and arotor 212. Thestator 211 is fixed to an inner surface of themotor case 22, and therotor 212 is fixed to a circumference of therotary shaft 210. Therotary shaft 210 is supported by themotor case 22 viabearings rotary shaft 210 is attached to the rotation center of theeccentric cam 35. - The
eccentric cam 35 is formed such that its rotation center is eccentric relative to the inner race of thebearing 34. So, when therotary shaft 210 rotates about its axis by the drive of themotor 21, theeccentric cam 35 rotates together with therotary shaft 210, and thus themovable member 30 reciprocates vertically within the operatingspace 105. With this, the volume of thepump chamber 100 periodically changes and a predetermined pump function is obtained. The amount of reciprocation of the movable member 30 (stroke amount) is determined by an eccentricity amount of theeccentric cam 35. - The
pump device 3 further includes a valve mechanism 50 (third valve). Thevalve mechanism 50 is attached to thedischarge port 102. Thevalve mechanism 50 has a function of limiting the outflow of gas from thedischarge port 102 at the time the operation of thepump device 3 is stopped. -
Fig. 3 is a perspective cross-sectional view showing the configuration of thevalve mechanism 50, andFig. 4 is a cross-sectional view thereof. Thevalve mechanism 50 includes avalve member 51 made of rubber and ametallic housing 52 that contains thevalve member 51. - The
housing 52 includes afirst end 521 connected to thedischarge port 102 of thecasing 10 and asecond end 522 connected to a pipe line (not shown) that communicates with theprocess unit 4. Aseal ring 54 is fitted to the circumference of thefirst end 521, and thefirst end 521 is hermetically attached to the inside of thedischarge port 102 by theseal ring 54. - Inside the
housing 52, aninner passage 523 that communicates between thefirst end 521 and thesecond end 522 is formed. Almost at the center portion of theinner passage 523, awall portion 53 including a plurality ofholes 531 at its center portion and circumference is formed perpendicularly to a wall surface of theinner passage 523, and thefirst end 521 and thesecond end 522 are capable of communicating with each other via thoseholes 531. - The
valve member 51 is constituted of an umbrella valve. Specifically, thevalve member 51 is formed into almost a disk shape and ashaft portion 511 formed at the center portion of thevalve member 51 is fitted to a center hole of thewall portion 53. Thus, thevalve member 51 is disposed in theinner passage 523. Anouter edge 512 of thevalve member 51 is elastically in contact with avalve seat 532 that is formed on a front surface of thewall portion 53 facing thesecond end 522, and stops the flow of the gas from thesecond end 522 side to thefirst end 521 side. Specifically, thevalve member 51 functions as a backflow prevention valve. - On the other hand, the
valve member 51 permits the gas to flow in the forward direction from thefirst end 521 side to thesecond end 522 side by opening the valve at a predetermined pressure or higher. In this case, as shown inFig. 4 , thevalve member 51 moves away from thevalve seat 532 because theouter edge 512 is elastically deformed to thesecond end 522 side, and a blocking state of theinner passage 523 by thevalve member 51 is released. Under a gas pressure lower than the predetermined pressure, theouter edge 512 is seated on thevalve seat 532, and the blocking state of theinner passage 523 is maintained. - A rubber material having resistance to various process gases is used for the
valve member 51. For example, in the case where methane, propane, or the like is used as process gas, rubber materials having resistance to hydrocarbon gas including methane and propane, such as nitrile rubber (NBR), hydrogenated nitrile rubber (HNBR), and fluoro-rubber (FKM), are used for thevalve member 51. The thickness or size of thevalve member 51 is not particularly limited and is set to a thickness or size enough to ensure a valve opening pressure compatible with various specifications. - Specifically, the valve opening pressure of the valve member 51 (minimum pressure required to open the valve member 51) is set to a pressure that is at least higher than the valve opening pressure (first pressure) of the
discharge valve 42. Thus, thevalve member 51 limits the flow of gas having a predetermined pressure (second pressure) or lower, the predetermined pressure (second pressure) being higher than the valve opening pressure of thevalve member 51. - The valve opening pressure of the
valve member 51 is determined by referring to the gas pressure PI supplied from thepressure source 2 of thepump system 1. In this embodiment, the valve opening pressure of thevalve member 51 is set to a pressure higher than the gas pressure PI of thepressure source 2. With this, even in the case where the gas pressure PI of thepressure source 2 is higher than the valve opening pressure of thedischarge valve 42, it is possible to block the outflow of gas from thedischarge port 102 to theprocess unit 4 when the operation of thepump device 3 is stopped and reliably prevent the outflow of gas to theprocess unit 4. - It should be noted that as will be described later, the valve opening pressure of the valve member may be set to a pressure lower than the gas pressure P2 of the
pressure source 2. - Next, a typical operation example of the
pump device 3 configured as described above will be described. - The
pump device 3 is driven by activation of themotor 21 of thedrive unit 20. The rotation speed of themotor 21 is controlled by thecontrol unit 5 so as to obtain a constant discharge flow rate based on a flowmeter provided on the discharge side of thepump device 3, for example. Themotor 21 reciprocates themovable member 30 in theoperating space 105 with predetermined strokes by rotating theeccentric cam 35 via therotary shaft 210. With this, thediaphragm 31 that partitions thepump chamber 100 moves up and down, and the volume of thepump chamber 100 changes periodically. - The
movable member 30 periodically changes the volume of thepump chamber 100 and thus alternately performs the suction of gas into thepump chamber 100 and the discharge of gas from thepump chamber 100. Specifically, the fuel gas of the pressure PI (for example, 2 kPa (gauge pressure)) is introduced into thepump chamber 100 via thesuction valve 41 from thepressure source 2 connected to thesuction port 101. The fuel gas introduced into thepump chamber 100 is compressed by the movable member in thepump chamber 100 and is boosted. Thus, thedischarge valve 42 and thevalve mechanism 50 are opened. By repetition of the above operation, the fuel gas of the pressure P2 (for example, 15 kPa (gauge pressure)) is discharged from thedischarge port 102 to theprocess unit 4. - Here, the
discharge valve 42 is opened at the time when the pressure within thepump chamber 100 reaches the valve opening pressure of thedischarge valve 42 or higher and permits the gas to flow from thepump chamber 100 to thedischarge port 102. So, when the gas is introduced into thepump chamber 100 from thesuction port 101 at a pressure equal to or higher than the valve opening pressure of thedischarge valve 42 when the operation of thepump device 3 is stopped, thedischarge valve 42 is opened and the flow of the gas toward thedischarge port 102 is formed. - In this regard, in the
pump device 3 of this embodiment, thevalve mechanism 50 is attached to thedischarge port 102. Thevalve mechanism 50 has a valve opening pressure that is higher than the gas pressure (P1) of thepressure source 2. So, even in the case where the gas of the pressure PI is introduced from thesuction port 101 to thepump chamber 100 when the operation of thepump device 3 is stopped, the flow of the gas is stopped by thevalve mechanism 50 and the outflow of the gas from thedischarge port 102 to theprocess unit 4 is prevented. In such a manner, since an unconsidered discharge of the gas when the operation is stopped is suppressed, it is possible to eliminate a possibility of causing a problem with a system. - Further, in this embodiment, the
valve mechanism 50 has the structure capable of continuously changing the degree of opening in accordance with an introduction pressure. With this, at the time the operation of thepump device 6 is restarted, thevalve mechanism 50 can be opened in accordance with a discharge pressure, and gas of a necessary flow rate can be supplied to theprocess unit 4 rapidly. -
Fig. 5 shows a time change of the discharge flow rate of thepump device 3 when the operation and stop of thepump device 3 are repeated under experimental conditions shown inFig. 6 . InFig. 6 , a is a buffer tank, b is a pressure gauge, c is suction piping, and d is a blower, which correspond to thepump device 3 of this embodiment. e is a pressure gauge, f is discharge piping, g is a fixed orifice, and h is a flowmeter. - As shown in
Fig. 5 , it was found that the minimum value of the discharge flow rate is zero and a function of confining gas by thevalve mechanism 50 normally works when the operation of thepump device 3 is stopped. Further, it was also found that the discharge flow rate of thepump device 6 is stably maintained to have a constant value and reproducibility is high. -
Fig. 7 shows experimental results that indicate a change in discharge flow rate of thepump device 6 with respect to a rotation speed control voltage (Vsp) input to themotor 21 of thepump device 6. A piping system in which thepump device 6 is incorporated is the same as the piping example shown inFig. 6 . - As shown in
Fig. 7 , it was found that after the operation of the pump device is started, the discharge of gas is started at the time the rotation speed reaches a predetermined rotation speed and its flow rate rises substantially in proportion to the driving rotation speed of the pump device. In such a manner, according to this embodiment, the function of confining gas and the stable control on the discharge flow rate can be achieved. -
Fig. 8 shows a pump device according to a second embodiment of the present invention. Hereinafter, a configuration different from that of the first embodiment will be mainly described, and the configurations that are the same as those in the embodiment described above will be denoted by the same reference numerals and description thereof will be omitted or simplified. - A
pump device 6 of this embodiment is different from that of the first embodiment described above in the configuration of avalve mechanism 60 attached to thedischarge port 102. Thevalve mechanism 60 includes avalve member 61 that configures an umbrella valve, and is provided in the inner passage of ahousing 62 in the same form as in the first embodiment shown inFigs. 3 and 4 . - The
valve mechanism 60 of this embodiment has a function common to the first embodiment, the function of limiting the outflow of gas having the valve opening pressure (first pressure) or higher of thedischarge valve 42 and the gas pressure PI (second pressure) or lower of thepressure source 2. However, thevalve mechanism 60 of this embodiment is different from that of the first embodiment in that thevalve mechanism 60 has a function of permitting gas to outflow from thedischarge port 102 to theprocess unit 4 while suppressing the outflow to a predetermined amount or less when the operation of thepump device 6 is stopped. - Specifically, the valve opening pressure of the
valve member 61 of this embodiment is set to a pressure lower than the gas pressure PI of thepressure source 2. Since thevalve mechanism 60 of the this embodiment has the structure capable of continuously changing the degree of opening in accordance with the gas pressure, the flow rate of gas outflowing to theprocess unit 4 side can be controlled in accordance with the pressure of gas introduced into thevalve mechanism 60. - In this case, a pressure required to fully open the
valve member 61 is set to a pressure higher than the gas pressure P1 of the pressure source 2 (for example, equal to or lower than the discharge pressure (P2) at the time of normal operation of the pump device 3). With this, the flow rate of gas having the valve opening pressure (first pressure) or higher of thedischarge valve 42 and the gas pressure P1 (second pressure) or lower of thepressure source 2 can be controlled by thevalve mechanism 60. - According to this embodiment, when the operation of the
pump device 6 is stopped, the flow rate of gas supplied from thepressure source 2 can be adjusted to a predetermined flow rate to be supplied to theprocess unit 4. With this, it is unnecessary to separately provide a throttle valve such as an orifice on an upstream or downstream side of thepump device 6, and this allows the number of components of the system to be reduced. This embodiment is suitably used for a system that needs to supply gas of a predetermined flow rate or lower to theprocess unit 4 also when the operation of thepump device 6 is stopped. -
Fig. 9 shows a pump device according to a third embodiment of the present invention. Hereinafter, a configuration different from that of the first embodiment will be mainly described, and the configurations that are the same as those in the embodiments described above will be denoted by the same reference numerals and description thereof will be omitted or simplified. - A
pump device 7 of this embodiment includes acasing 70 including apump body 11, apump head 72, and apump head cover 73. Asuction port 101 and adischarge port 102 are formed in thepump head 72. Thevalve mechanism 50 described in the first embodiment is attached to thedischarge port 102. - Further, a suction passage T1, a discharge passage T2, and a
buffer tank 721 are formed in thepump head 72. At least a part of each of those passages is exposed to the outside from the upper surface of thepump head 72 and is covered with thepump head cover 73 via a seal member to be isolated from open air. - In general, a diaphragm pump structurally generates pulsations in discharge gas. In the case where the driving rotation speed of the pump is controlled based on a measured value of the flow rate of discharge gas, when a pulsation is large, a correct flow rate cannot be measured and the drive control of the pump becomes unstable. Further, in the case where the discharge gas is fuel gas, there is a possibility that the pulsations cause unstable combustion or incomplete combustion.
- In this regard, the
pump device 7 of this embodiment includes thebuffer tank 721 between the discharge passage T2 and thedischarge port 102. Thebuffer tank 721 forms aspace portion 74 between a discharge valve 42 (discharge passage T2) and thevalve mechanism 50 by expanding a part of a flow path that communicates with the discharge valve 42 (discharge passage T2) and thevalve mechanism 50. Thebuffer tank 721 has a function of buffering the pulsations of gas discharged from thedischarge valve 42. - According to the
pump device 7 of this embodiment, it is possible to reduce the pulsations of gas discharged from thevalve mechanism 50 and discharge gas at a stable flow rate. Further, in the case where the drive of thepump device 7 is controlled based on the discharge flow rate, it is possible to perform stable drive control of thepump device 7. Further, since the pump and the buffer tank are integrated, it is not necessary to separately provide a buffer tank in the gas flow path of the pump system, and the system configuration can be simplified. - The volume of the
space portion 74 of thebuffer tank 721 is determined based on the pulsations (pressure range) of the gas discharged from thedischarge valve 42.Fig. 10 shows results of an experiment performed by the inventors of the present invention and shows a relationship between a buffer volume (cc) and a pressure range of gas discharged from thedischarge port 102. As shown inFig. 10 , as the volume of thespace portion 74 becomes larger, the pressure range can be made smaller. For example, when the volume of thespace portion 74 is set to 120 cc or more, the pulsation range can be reduced to 0.75 kPa or less. -
Fig. 10 shows a pump device according to a fourth embodiment of the present invention. Hereinafter, a configuration different from that of the first embodiment will be mainly described, and the configurations that are the same as those in the embodiments described above will be denoted by the same reference numerals and description thereof will be omitted or simplified. - A
pump device 8 of this embodiment includes acasing 80, adrive unit 20, and abuffer tank 81. Thecasing 80 includes asuction port 101 and adischarge port 102, boosts gas suctioned from thesuction port 101 in a pump chamber (not shown), and discharges the boosted gas from thedischarge port 102 via thebuffer tank 81. -
Fig. 11 is a cross-sectional view of thebuffer tank 81 and thedischarge port 102. Aspace portion 74 having a predetermined volume is formed within thebuffer tank 81 and reduces pulsations of the discharge gas. Thedischarge port 102 communicates with thespace portion 74, and avalve member 51 is attached to the inside of thedischarge port 102. Thevalve member 51 has the same configuration as that of the first embodiment and has a function of limiting the outflow of gas having a predetermined pressure or less. - Also in this embodiment configured as described above, the same actions and effects as those of the embodiments described above can be obtained. According to the
pump device 8 of this embodiment, since thevalve member 51 as a valve mechanism is supported by thecasing 80, the number of components can be reduced. - It should be noted that
Figs. 13 to 18 each show an outer appearance of thepump device 8.Fig. 13 is a front view,Fig. 14 is a back view,Fig. 15 is a plan view,Fig. 16 is a bottom view,Fig. 17 is a right side view, andFig. 18 is a left side view. - Hereinabove, the embodiments of the present invention have been described, but the present invention is not limited to the embodiments described above and can be variously modified without departing from the gist of the present invention as a matter of course.
- For example, in the embodiments described above, the valve mechanism that limits the flow of the gas having a predetermined pressure or lower is attached to the discharge port, but the present invention is not limited thereto. For example, the valve mechanism may be provided on a discharge passage between the discharge valve and the discharge port.
- Further, the valve member that constitutes the valve mechanism is not limited to the umbrella valve and may be constituted of a ball valve or a butterfly valve, for example.
- Furthermore, in the embodiments described above, the pump device is constituted of the diaphragm pump, but the present invention is not limited thereto and can also be applied to another pump device such as a roots pump. In the case of a roots pump, the movable member that changes the volume of the pump chamber corresponds to rotors disposed to be opposed to each other.
-
- 1
- pump system
- 2
- pressure source
- 3, 6, 7, 8
- pump device
- 4
- process unit
- 10, 70, 80
- casing
- 20
- drive unit
- 30
- movable member
- 31
- diaphragm
- 41
- suction valve
- 42
- discharge valve
- 50, 60
- valve mechanism
- 51, 61
- valve member
- 74
- space portion
- 100
- pump chamber
- 101
- suction port
- 102
- discharge port
Claims (8)
- A pump device (3; 6; 7; 8), comprising:a casing (10; 70; 80) including
a suction port (101), a discharge port (102), and a pump chamber (100) that can communicate with the suction port (101) and the discharge port (102);a movable member (30) that is movable within the casing (10; 70; 80) and alternately performs suction of a gas into the pump chamber (100) and discharge of the gas from the pump chamber (100);a first valve that is attached between the suction port (101) and the pump chamber (100) and permits the gas to flow from the suction port (101) to the pump chamber (100);a second valve that is attached between the pump chamber (100) and the discharge port (102) and permits the gas to flow from the pump chamber (100) to the discharge port (102) in a case where the gas of the pump chamber (100) has a first pressure or higher; characterised in that a third valve that is attached to the discharge port (102) and limits a flow of the gas toward the discharge port (102) from the suction port (101) in a case where the gas between the suction port (101) and the discharge port (102) has a second pressure or lower, the second pressure being higher than the first pressure. - The pump device (3; 6; 7; 8) according to claim 1, wherein
the third valve includes a valve member (51; 61) that continuously changes the degree of opening in accordance with a pressure equal to or higher than the first pressure and equal to or lower than the second pressure. - The pump device (3; 6; 7; 8) according to claim 2, wherein
the valve member (51; 61) is an umbrella valve. - The pump device (3; 6; 7; 8) according to claim 1, wherein
the casing (10; 70; 80) further includes a space portion obtained by expanding a part of a flow path that communicates between the second valve and the third valve. - The pump device (3; 6; 7; 8) according to claim 1, wherein
the movable member (30) includes a diaphragm that is deformable and partitions the pump chamber (100). - A pump system (1), comprising:a pump device (3; 6; 7; 8) includinga casing (10; 70; 80) includinga suction port (101) that communicates with a pressure source, a discharge port (102) that communicates with a process unit, and a pump chamber (100) that can communicate with the suction port (101) and the discharge port (102),a movable member (30) that is movable within the casing (10; 70; 80) (100) and alternately performs suction of a gas into the pump chamber (100) and discharge of the gas from the pump chamber (100),a first valve that is attached between the suction port (101) and the pump chamber (100) and permits the gas to flow toward the pump chamber (100) from the suction port (101),a second valve that is attached between the pump chamber (100) and the discharge port (102) and permits the gas having a first pressure or higher to flow toward the discharge port (102) from the pump chamber (100), anda third valve that is attached to the discharge port (102) and limits a flow of the gas having a second pressure or lower to flow toward the discharge port (102) from the suction port (101), the second pressure being higher than the first pressure;a pressure source (2) that is connected to the suction port (101) and supplies the gas having the second pressure or lower to the pump device (3; 6; 7; 8); anda process unit (4) that is connected to the discharge port (102) and processes the gas discharged from the pump device (3; 6; 7; 8).
- The pump system (1) according to claim 6, wherein
the third valve includes a valve member (51; 61) that blocks the flow of the gas having the second pressure or lower. - The pump system (1) according to claim 6, wherein
the third valve includes a valve member (51; 61) that continuously changes the degree of opening in accordance with a pressure equal to or higher than the first pressure and equal to or lower than the second pressure.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
PCT/JP2012/001023 WO2013121463A1 (en) | 2012-02-16 | 2012-02-16 | Pump device and pump system |
Publications (3)
Publication Number | Publication Date |
---|---|
EP2816233A1 EP2816233A1 (en) | 2014-12-24 |
EP2816233A4 EP2816233A4 (en) | 2015-12-23 |
EP2816233B1 true EP2816233B1 (en) | 2017-10-18 |
Family
ID=48983635
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP12868917.1A Active EP2816233B1 (en) | 2012-02-16 | 2012-02-16 | Pump device and pump system |
Country Status (4)
Country | Link |
---|---|
US (1) | US20160003228A1 (en) |
EP (1) | EP2816233B1 (en) |
CA (1) | CA2863775A1 (en) |
WO (1) | WO2013121463A1 (en) |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2018503764A (en) * | 2014-11-27 | 2018-02-08 | プロフタガレン アクチエボラグProvtagaren Ab | Low flow pump control |
DK201570293A1 (en) * | 2015-05-19 | 2016-12-12 | Nel Hydrogen As | Diaphragm compressor with an oblong shaped chamber |
JP7144727B2 (en) * | 2018-08-08 | 2022-09-30 | セイコーエプソン株式会社 | Diaphragm compressor, projector, cooler, and fluid compression method |
CN208950819U (en) * | 2018-09-30 | 2019-06-07 | 深圳市大疆软件科技有限公司 | Diaphragm pump and agriculture unmanned plane |
Family Cites Families (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB470354A (en) * | 1936-03-04 | 1937-08-13 | Exactor Control Company Ltd | Improvements relating to fuel pumps, particularly for engine priming |
US2593255A (en) * | 1946-10-26 | 1952-04-15 | George F Bowman | High-pressure diaphragm pump |
ATE35442T1 (en) * | 1983-04-08 | 1988-07-15 | Cash Eng Co Pty Ltd | COMPRESSOR CONTROL SYSTEM. |
US4681518A (en) * | 1985-02-19 | 1987-07-21 | The Coca-Cola Company | Single-acting, gas operated pump |
JPH03127089U (en) * | 1990-03-31 | 1991-12-20 | ||
US5507318A (en) * | 1994-10-04 | 1996-04-16 | Walbro Corporation | Umbrella check valves |
JP2003307177A (en) * | 2002-04-12 | 2003-10-31 | Japan Steel Works Ltd:The | Hydrogen compressing device |
JP3893322B2 (en) * | 2002-05-24 | 2007-03-14 | 日機装株式会社 | Reciprocating pump |
JP2005023788A (en) * | 2003-06-30 | 2005-01-27 | Kohoku Kogyo Kk | Pump |
WO2006017375A2 (en) * | 2004-08-06 | 2006-02-16 | Ultracell Corporation | Method and system for controlling fluid delivery in a fuel cell |
JP2008261233A (en) * | 2007-04-10 | 2008-10-30 | Nippon Soken Inc | High pressure fuel pump |
JP5052995B2 (en) | 2007-08-21 | 2012-10-17 | アルバック機工株式会社 | Diaphragm pump |
JP5412243B2 (en) * | 2009-11-06 | 2014-02-12 | 株式会社日立産機システム | Booster compressor |
-
2012
- 2012-02-16 CA CA2863775A patent/CA2863775A1/en not_active Abandoned
- 2012-02-16 WO PCT/JP2012/001023 patent/WO2013121463A1/en active Application Filing
- 2012-02-16 EP EP12868917.1A patent/EP2816233B1/en active Active
- 2012-02-16 US US14/378,735 patent/US20160003228A1/en not_active Abandoned
Non-Patent Citations (1)
Title |
---|
None * |
Also Published As
Publication number | Publication date |
---|---|
EP2816233A1 (en) | 2014-12-24 |
EP2816233A4 (en) | 2015-12-23 |
US20160003228A1 (en) | 2016-01-07 |
WO2013121463A1 (en) | 2013-08-22 |
CA2863775A1 (en) | 2013-08-22 |
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