Safety Hydraulic Dump for a Cryogenic Pump
20180058218 ยท 2018-03-01
Assignee
Inventors
- Sunil J. Bean (Woodridge, IL, US)
- Alan R. Stockner (Metamora, IL, US)
- Mingchun Dong (Bloomington, IL, US)
Cpc classification
F04B2015/081
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F04B23/021
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F04B9/103
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
International classification
F01B23/08
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F01B1/01
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F04B9/103
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F01B31/28
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F04B15/08
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F01B25/00
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
Abstract
A cryogenic fluid pump includes a drive assembly and a pumping assembly. The drive assembly includes a cylinder. The cylinder includes an annular dump channel formed in and extending about an interior wall of the cylinder. A piston is reciprocatable within the cylinder between a first and second position. A hydraulic pressure chamber is defined by the cylinder and the piston. The piston includes an axial spill passage in communication with the pressure chamber and a transverse spill passage in communication with the axial spill passage. The transverse spill passage includes a piston dump port which is sealed to the cylinder in the first position and in the second position unsealed to the cylinder to permit fluid exit from the pressure chamber. The second position includes an over travel state and the dump area of the piston dump port when unsealed to the cylinder increases as the piston advances.
Claims
1. A cryogenic fluid pump, comprising: a drive assembly and a pumping assembly, the drive assembly including a cylinder, the cylinder including an annular dump channel that is formed in and extends about an interior wall of the cylinder; a piston reciprocatable within the cylinder between a first position and a second position; and a hydraulic pressure chamber defined by the cylinder and the piston; the piston including at least one axial spill passage in communication with the hydraulic pressure chamber and a transverse spill passage in communication with the at least one axial spill passage, the transverse spill passage including a piston dump port, the piston dump port sealed to the cylinder in the first position and in the second position unsealed to the cylinder to permit fluid exit from the hydraulic pressure chamber, wherein the second position includes an over travel state and wherein the dump area of the piston dump port unsealed to the cylinder continues to increase as the piston advances in the over travel state.
2. The cryogenic fluid pump of claim 1, wherein the piston dump port is in communication with the annular dump channel in the second position.
3. The cryogenic fluid pump of claim 2, wherein the at least one axial spill passage extends less than half the axial length of the piston.
4. The cryogenic fluid pump of claim 1, wherein the at least one axial spill passage includes a pair of axial spill passages.
5. The cryogenic fluid pump of claim 1, wherein the piston includes a transverse width and the transverse spill passage extends the entire transverse width of the piston.
6. The cryogenic fluid pump of claim 1, wherein the annular dump channel is a rectangular groove.
7. The cryogenic fluid pump of claim 1, wherein the at least one axial spill passage extends more than half the axial length of the piston.
8. The cryogenic fluid pump of claim 7, wherein the piston dump port clears an end portion of the cylinder in the second position, wherein the second position corresponds to greater than or equal to 100 percent of an end of stroke position.
9. The cryogenic fluid pump of claim 8, wherein a top of the piston clears the annular dump channel permitting fluid to exit from the hydraulic pressure chamber directly into the annular dump channel, wherein the second position includes the over travel state.
10. The cryogenic fluid pump of claim 1, wherein the piston dump port includes one of a triangular cross section and a U-shaped cross section.
11. A pumping system for providing a cryogenic fluid for use as a fuel for an engine, comprising: an electronic controller; a cryogenic pump operably associated with the electronic controller, wherein operation of the cryogenic pump is responsive to pump commands from the electronic controller; the cryogenic pump having a plurality of pumping elements, each of the plurality of pumping elements comprising: a drive assembly and a pumping assembly, the pumping assembly operably responsive to the drive assembly, the drive assembly including a cylinder, the cylinder including an annular dump channel that is formed in and extends about an interior wall of the cylinder; a piston reciprocatable within the cylinder between a first position and a second position; and a hydraulic pressure chamber defined by the cylinder and the piston; the piston including at least one axial spill passage in communication with the hydraulic pressure chamber and a transverse spill passage in communication with the at least one axial spill passage, the transverse spill passage including a piston dump port, the piston dump port sealed to the cylinder in the first position and in the second position unsealed to the cylinder to permit fluid exit from the hydraulic pressure chamber, wherein the second position includes an over travel state and wherein the dump area of the piston dump port unsealed to the cylinder continues to increase as the piston advances in the over travel state.
12. The cryogenic fluid pump of claim 11, wherein the piston dump port is in communication with the annular dump channel in the second position.
13. The cryogenic fluid pump of claim 12, wherein the at least one axial spill passage extends less than half the axial length of the piston.
14. The cryogenic fluid pump of claim 11, wherein the at least one axial spill passage includes a pair of axial spill passages.
15. The cryogenic fluid pump of claim 11, wherein the piston includes a transverse width and the transverse spill passage extends the entire transverse width of the piston.
16. The cryogenic fluid pump of claim 11, wherein the at least one axial spill passage extends more than half the axial length of the piston.
17. The cryogenic fluid pump of claim 16, wherein the piston dump port clears an end portion of the cylinder in the second position, wherein the second position corresponds to greater than or equal to 100 percent end of an end of stroke position.
18. The cryogenic fluid pump of claim 17, wherein a top of the piston clears the annular dump channel permitting fluid to exit from the hydraulic pressure chamber directly into the annular dump channel, wherein the second position includes the over stroke state.
19. The cryogenic fluid pump of claim 11, wherein the piston dump port is includes one of a triangular cross section and a U-shaped cross section.
20. A cryogenic fluid pump, comprising: a plurality of pumping elements in communication with an electronic controller, each of the pumping elements including: a drive assembly including an electromechanical actuator having a pin associated therewith, the pin arranged in a bore having a fluid supply passage, a spool valve supply outlet, and a drain outlet, wherein the pin is moveable between a deactivation position, in which the hydraulic oil supply passage is fluidly connected with the spool valve supply outlet, and an activation position, in which the spool valve supply outlet is fluidly connected with the drain outlet; the drive assembly including a cylinder, the cylinder including an annular dump channel that is formed in and extends about an interior wall of the cylinder, a piston reciprocatable within the cylinder between a first position and a second position, and a hydraulic pressure chamber defined by the cylinder and the piston, the piston including at least one axial spill passage in communication with the hydraulic pressure chamber and a transverse spill passage in communication with the at least one axial spill passage, the transverse spill passage including a piston dump port, the piston dump port sealed to the cylinder in the first position and in the second position unsealed to the cylinder to permit fluid exit from the hydraulic pressure chamber, wherein the second position includes an over travel state and wherein the dump area of the piston dump port unsealed to the cylinder continues to increase as the piston advances in the over travel state; the drive assembly associated with and configured to selectively activate one end of a pushrod in response to a command by the electronic controller; and a pump assembly associated with an opposite end of the pushrod wherein the pump assembly is activated for pumping a fluid by the drive assembly; wherein the electronic controller is configured to selectively activate the drive assembly such that a flow of fluid from the cryogenic fluid pump results from successive activations thereof at selected dwell times between activations.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
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DETAILED DESCRIPTION
[0020] This disclosure relates to machines with engines using a gaseous fuel (e.g., methane of other hydrocarbon mixtures commonly known as natural gas or petroleum gas) source such as direct injection gas (DIG) or indirect injection gas engines using diesel or spark ignition. More particularly, the disclosure relates to a hydraulic drive system for a cryogenic liquid natural gas (LNG) pump that supplies pressurized natural gas fuel to an engine. A schematic diagram of a DIG, engine system 100, which in the illustrated embodiment uses liquid diesel fuel as the ignition source, is shown in
[0021] The fuel injector 104 is connected to a high-pressure gaseous fuel rail 106 via a high-pressure gaseous fuel supply line 108 and to a high-pressure liquid fuel rail 110 via a liquid fuel supply line 112. In the illustrated embodiment, the gaseous fuel is natural or petroleum gas that is provided through the high-pressure gaseous fuel supply line 108 at a pressure of between about 10-50 MPa, and the liquid fuel is diesel, which is maintained within the high-pressure liquid fuel rail 110 at about 15-100 MPa, but any other pressures or types of fuels may be used depending on the operating conditions of each engine application. The liquid fuel can be any hydrocarbon based fuel; for example DME (Di-methyl Ether), biofuel, MDO (Marine Diesel Oil), or HFO (Heavy Fuel Oil).
[0022] Whether the engine system 100 is installed in a mobile or a stationary application, each of which is contemplated, the gaseous fuel may be stored in a liquid state in a tank 114, which can be a cryogenic storage tank that is pressurized at a relatively low pressure, for example, atmospheric, or at a higher pressure. In the illustrated embodiment, the tank 114 is insulated to store liquefied natural gas (LNG) at a temperature of about 160 C. (256 F.) and a pressure that is between about 100 and 1750 kPa, but other storage conditions may be used. The tank 114 further includes a pressure relief valve 116. In the description that follows, a DIG engine system embodiment is used for illustration, but it should be appreciated that the systems and methods disclosed herein are applicable to any machine, vehicle or application that uses cryogenically stored gas, for example, a locomotive in which the tank 114 may be carried in a tender car.
[0023] Relative to the particular embodiment illustrated, during operation, LNG from the tank is pressurized, still in a liquid phase, in a pump 118, which raises the pressure of the LNG while maintaining the LNG in a liquid phase. The pump 118 is configured to selectively increase the flow of the LNG that can vary in response to a command signal provided to the pump 118 from an electronic controller 120. The pump 118 is shown external to the tank 114 in
[0024] The pressurized LNG provided by the pump 118 is heated in a heat exchanger 122. The heat exchanger 122 provides heat to the compressed LNG to change the LNG phase to a gaseous/supercritical state which is more suitable for combustion. In one exemplary application, the LNG may enter the heat exchanger 122 at a temperature of about 160 C., a density of about 430 kg/m.sup.3, an enthalpy of about 70 kJ/kg, and a viscosity of about 169 Pa s as a liquid, and exit the heat exchanger at a temperature of about 50 C., a density of about 220 kg/m.sup.3, an enthalpy of about 760 kJ/kg, and a viscosity of about 28 Pa s. It should be appreciated that the values of such representative state parameters may be different depending on the particular composition of the fuel being used. In general, the fuel is expected to enter the heat exchanger in a cryogenic, liquid state, and exit the heat exchanger in a supercritical gas state, which is used herein to describe a state in which the fuel is gaseous but has a density that is between that of its gaseous and liquid phases.
[0025] The heat exchanger 122 may be any known type of heat exchanger or heater for use with LNG. In the illustrated embodiment, the heat exchanger 122 is a jacket water heater that extracts heat from engine coolant. In alternative embodiments, the heat exchanger 122 may be embodied as an active heater, for example, a fuel fired or electrical heater, or may alternatively be a heat exchanger using a different heat source, such as heat recovered from exhaust gases of the engine 102, a different engine belonging to the same system such as what is commonly the case in locomotives, waste heat from an industrial process, and other types of heaters or heat exchangers. In the embodiment shown in
[0026] Liquid fuel, or in the illustrated embodiment diesel fuel, is stored in a fuel reservoir 136. From there, fuel is drawn into a fuel pump 138 through a filter 140. The fuel pump 138 may have a variable flow capability to provide fuel to the engine at a variable rate depending on the operating mode of the engine. The rate of fuel provided by the fuel pump 138 can be controlled in response to a command signal from the electronic controller 120. Pressurized fuel from the fuel pump 138 is provided to the high-pressure liquid fuel rail 110. Similarly, the pump 118 has a variable supply capability that is responsive to a signal from the electronic controller 120.
[0027] Contaminants may be removed from the natural gas exiting the heat exchanger 122 by a filter 124. As can be appreciated, the natural gas passing through the filter 124 may be present in more than one phase such as gas or liquid. An optional natural gas accumulator 126 may collect filtered gas upstream of a pressure regulator 128 that can selectively control the pressure of gas provided to the high-pressure gaseous fuel rail 106 that is connected to the high-pressure gaseous fuel supply line 108. To operate the pump 118, a hydraulic pump 150 having a variable displacement and selectively providing pressurized hydraulic fluid to the pump 118 via a valve system 152 is used. Operation of the hydraulic pump 150 is controlled by an actuator 154 that responds to commands from the electronic controller 120. The valve system 152 also operates in response to commands from the controller 120. It will be appreciated that while system 100 illustrates one or more embodiment, other configurations are contemplated.
[0028] A section view of the tank 114 having the pump 118 at least partially disposed therein is shown in
[0029] The pump 118 in the illustrated embodiment includes a pump flange 220 that supports the pump 118 on the mounting flange 216 of the tank 114. A partially sectioned view of the pump 118, removed from the tank 114, is also shown in
[0030] In the illustrated embodiment, the pushrods 304, shown in cross section in
[0031] The pressurized hydraulic fluid to activate the piston 314 is provided in the space behind the piston, and is also vented, by the selective positioning of a spool valve 322, which is shown in two operating positions in
[0032] The spool valve 322 in the illustrated embodiment includes a spool valve element 324 that is reciprocally mounted and operates within a bore 326. The bore 326, which accommodates the spool valve element 324, is fluidly connected to a fluid supply passage 328, which supplies pressurized fluid to move the piston 314. For example, as shown in
[0033] The bore 326 is also fluidly connected to a vent passage 330 (partially shown in
[0034] In the illustrated embodiment, the spool valve element 324 at an energized condition is disposed in the fill position (
[0035] More specifically, during operation, depending on the activation state of the solenoid 336, the position of the pin 338 within the pin guide 346 operates between an activation position and a drain position. In the activation position, a lower seat valve 347 opens as the armature 344 moves upward, which places the spool valve supply outlet 352 in fluid communication with the drain outlet 354, which, as shown in
[0036] Operation of the actuator 334 depends on the presence of electrical power, which is selectively provided by the electronic controller 120 (
[0037] Turning to
[0038] For purposes of the present disclosure, travel of the piston 314 within a specified range, i.e., from 0-100 percent of the designed travel will be considered a normal or specified travel state with 100 percent the end of specified travel. Travel of the piston 314 beyond a specified range, i.e., greater than 100 of the designed travel will be considered an over travel state.
[0039] Specifically, piston 314 reciprocates in cylinder 316 and, in part, defines a hydraulic pressure chamber 410, defined at least in part by the top 412 of the piston, that is provided with fluid from activation passage 318. Piston 314 includes at least one axial spill passage 414, which extends axially through the piston in communication with the hydraulic pressure chamber 410. Two axial spill passages 414 are shown. Each axial spill passage 414 may extend through the piston 314 less than the axial length of the piston. In one embodiment, the axial spill passage 414 may extend through the piston 314 about a fourth of the axial length of the piston. The at least one axial spill passage 414 is in communication with a transverse spill passage 416 that extends transversely to the axis of the piston 314 and opens to a relief pressure area, for example, on the outside of the piston. The transverse spill passage 416 has a piston dump port 418, which forms the opening of the passage to the outside of the piston 314. The transverse spill passage 416 can have any cross-sectional shape to supply sufficient flow of fluid to the piston dump port 418. The piston dump port 418, in the illustrated embodiments, may have a non-round cross-section to meter the flow area therethrough such that flow of fluid is dumped at a higher rate that can be accomplished with a circular port opening. Some examples of piston dump ports 418 are shown in detail in
[0040] The cylinder 316 includes an annular dump channel 420. The annular dump channel 420 may be a groove formed in the inward facing inside wall of the cylinder 316. The annular dump channel 420 is in communication with the transverse spill passage 416 through the piston dump port 418 when the piston 314 is at its expected fully-extended travel position illustrated at pumping element example 400B and not in communication with the transverse spill passage when at an intermediate travel position or its fully-retracted position as shown at pumping element example 400A. When the piston dump port 418 and annular dump channel 420 are in fluid communication with the cylinder dump port 422, a passage is provided for fluid to exit the fluid chamber 410. The cross sectional shape of the piston dump port 418 in combination with the annular dump channel 420 permits a relief or dumping of hydraulic pressure from the hydraulic pressure chamber 410.
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[0044] Embodiment 418a has a triangular configuration such that the cross sectional area of the passage available for fluid to flow through is small at the beginning of fluid exit at 550 with a relatively small or first dump port area shown at 554. The port area increases in a quadratic fashion as the piston dump port 418a includes the port area shown at 556. In contrast to a circular port area, where the port area increases initially at a fast rate and then increases at a decreasing rate (less than linear) describing a sigmoid curve, the area of the piston dump port 418a increases at a greater than linear rate. In particular, the port dump area 554, 556 continues to increase as the piston progresses in an over travel state.
[0045] Embodiment 418b and 418c is a U-shape such that flow through is a small amount at the beginning of fluid exit at 550 with a semicircular dump port area shown at 554. The port area increases as the piston dump port 418a includes the rectangular areas shown at 556. Embodiment 418c has a lesser total throughput at maximum port area of combined port areas 554 and 556. The rectangular area 556 provides a linear rate of fluid exit. The port dump area 554, 556 continues to increase as the piston progresses in an over travel state.
[0046] Embodiment 418d is initially the same as 418c including a U-shape such that flow through is a small amount at the beginning of fluid exit at 550 with a semicircular dump port area shown at 554. The port area increases as the piston dump port 418d includes the rectangular areas shown at 556. The rectangular area 556 provides a linear rate of fluid exit. The area shown at 556 includes a flared portion at the upper end 552 thereof which permits a large expansion of fluid flow at the fully open and maximum dump port area which represents an increased rate of flow beyond the linear rate of portion 556. The port dump area 554, 556 continues to increase as the piston progresses in an over travel state.
[0047] Embodiment 418e is initially the same as 418d including a semicircular shape such that flow through is a small amount at the beginning of fluid exit at 550 with a semicircular dump port area shown at 554. The port area increases as the piston dump port 418d includes the triangular area shown at 556. The triangular area 556 provides more than a linear rate of fluid exit. The port dump area 554, 556 continues to increase as the piston progresses in an over travel state.
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INDUSTRIAL APPLICABILITY
[0049] The present disclosure is applicable to any type of application that involves a hydraulic dump to prevent piston over travel. The present disclosure presents several embodiments of dump port configurations that function to protect a cryogenic pump from over travel states. In particular, the embodiments presented herein provide an increase of dump area vs. piston travel in an over travel state.
[0050] It will be appreciated that the foregoing description provides examples of the disclosed system and technique. However, it is contemplated that other implementations of the disclosure may differ in detail from the foregoing examples. All references to the disclosure or examples thereof are intended to reference the particular example being discussed at that point and are not intended to imply any limitation as to the scope of the disclosure more generally. All language of distinction and disparagement with respect to certain features is intended to indicate a lack of preference for those features, but not to exclude such from the scope of the disclosure entirely unless otherwise indicated.
[0051] Recitation of ranges of values herein are merely intended to serve as a shorthand method of referring individually to each separate value falling within the range, unless otherwise indicated herein, and each separate value is incorporated into the specification as if it were individually recited herein. All methods described herein can be performed in any suitable order unless otherwise indicated herein or otherwise clearly contradicted by context.