This patent disclosure relates generally to pumps and, more particularly, to cryogenic fuel pumps for mobile applications.
Many large mobile machines such as mining trucks, locomotives, marine applications and the like have recently begun using alternative fuels, alone or in conjunction with traditional fuels, to power their engines. For example, large displacement engines may use a gaseous fuel, alone or in combination with a traditional fuel such as diesel, to operate. Because of their relatively low densities, gaseous fuels, for example, natural gas or petroleum gas, are carried onboard vehicles in liquid form. These liquids, the most common including liquefied natural gas (LNG) or liquefied petroleum gas (LPG), are cryogenically stored in insulated tanks on the vehicles, from where a desired quantity of fuel is pumped, evaporated, and provided to fuel the engine.
The pumps that are typically used to deliver the LNG to the engine of the machine include pistons, which deliver the LNG to the engine. Such piston pumps, which are sometimes also referred to as cryogenic pumps, will often include a single piston that is reciprocally mounted in a cylinder bore. The piston is moved back and forth in the cylinder to draw in and then compress the LNG. Power to move the piston may be provided by different means, the most common being electrical, mechanical or hydraulic power.
One example of a cryogenic pump can be found in U.S. Pat. No. 7,293,418 (the '418 patent), which describes a cryogenic, single-element pump for use in a vehicle. The pump discharges into an accumulator that is located within the tank, and uses a single piston pump that is connected to a drive section via a piston rod. The drive section is disposed outside of the tank.
Pumps such as the pump described in the '418 patent are generally large, heavy and complex, which are due, in part, to the large operating pressures and high volumes of fluid that must be delivered to operate a large displacement engine. Because of the nature of their operation, in that a quantity of fluid is delivered by each stroke, typical systems also require various pressure accumulators and regulators to smooth the supply of gaseous fuel to the engine, which further burdens the vehicles with additional components, cost and complexity.
The present disclosure is generally directed to a hydraulically driven cryogenic pump comprising multiple plunging pumping elements. The cryogenic pump may be disposed at least partially within an LNG tank. The disclosed systems and method are generally more cost effective than previously proposed system, in that they may be configured without the need to use accumulators, regulators and boost pumps. This, and other aspects, allow an overall reduction of the gas delivery system's size, weight and complexity, and also durability.
The disclosure, therefore, describes, in one aspect, a cryogenic pump. The cryogenic pump includes a plurality of pumping elements, each of which has an actuator portion that is associated with, and configured to, selectively activate one end of a pushrod in response to a command by an electronic controller. Each pumping element further includes an activation portion associated with an opposite end of the pushrod, and a pumping portion associated with the activation portion. For each of the plurality of pumping elements, the pumping portion is activated for pumping a fluid by the activation portion, which activation portion is activated by the actuator portion. The electronic controller is configured to selectively activate each of the plurality of pumping elements such that a flow of fluid from the cryogenic fluid pump results from successive activations of the plurality of pumping elements at selected dwell times between activations.
In another aspect, the disclosure describes a method for operating a cryogenic pump having a plurality of pumping elements included therewith, each of the plurality of pumping elements being responsive to a corresponding pumping command from an electronic controller. The method includes determining, in the electronic controller, a desired flow rate for fluid pumped by the cryogenic pump, and also determining, in the electronic controller, a frequency and dwell time of pumping element activations based on the desired flow rate. The method further includes commanding with the electronic controller each of the plurality of pumping elements to perform a corresponding pumping stroke, such that an aggregate of the fluid pumped by each of the corresponding pumping strokes approaches the desired flow rate.
In yet another aspect, the disclosure describes a pumping system for providing a cryogenic fluid for use as a fuel for an engine. The pumping system includes an electronic controller, a hydraulic pump operably associated with the electronic controller, wherein operation of the hydraulic pump is responsive to pump commands from the electronic controller, and a cryogenic pump having a plurality of pumping elements. Each of the plurality of pumping elements includes an actuator portion that is associated with and configured to selectively activate one end of a pushrod in response to a command by the electronic controller. The actuator portion is powered by hydraulic fluid provided at a pressure by the hydraulic pump. Each of the plurality of pumping elements further includes an activation portion associated with an opposite end of the pushrod, and a pumping portion associated with the activation portion. For each of the plurality of pumping elements, the pumping portion is activated for pumping a fluid by the activation portion, which activation portion is activated by the actuator portion. The electronic controller is configured to selectively activate each of the plurality of pumping elements such that a flow of fluid from the cryogenic fluid pump results from continuous activations of the plurality of pumping elements at selected dwell times between activations of successive pumping elements.
This disclosure relates to engines using a gaseous fuel source such as direct injection gas (DIG) or indirect injection gas engines using diesel or spark ignition. More particularly, the disclosure relates to an embodiment for an engine system that includes a gaseous fuel storage tank having a pump that supplies cryogenically stored fluid to fuel an engine. A schematic diagram of a DIG, engine system 100, which in the illustrated embodiment uses diesel as the ignition source, is shown in
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. It is noted that although reference is made to the fuels present in the high-pressure gaseous fuel supply line 108 and the high-pressure liquid fuel rail 110 using the words “gaseous” or “liquid,” these designations are not intended to limit the phase in which is fuel is present in the respective rail and are rather used solely for the sake of discussion of the illustrated embodiment. For example, the fuel provided at a controlled pressure within the high-pressure gaseous fuel supply line 108, depending on the pressure at which it is maintained, may be in a liquid, gaseous or supercritical phase. Additionally, 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).
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.
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 pressure of the LNG to a pressure that can vary in response to a pressure command signal provided to the pump 118 from an electronic controller 120. The pump 118 is shown external to the tank 114 in
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 reduce density and viscosity while increasing its enthalpy and temperature. 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/m3, an enthalpy of about 70 kJ/kg, and a viscosity of about 169 μPa s as a liquid, and exit the heat exchanger at a temperature of about 50° C., a density of about 220 kg/m3, an enthalpy of about 760 kJ/kg, and a viscosity of about 28 μPa 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 vapor and liquid phases.
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
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.
Contaminants may be removed from the gas exiting the heat exchanger 122 by a filter 124. As can be appreciated, the gas passing through the filter 124 may include gas present in more than one phase such as gas or liquid. An optional 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.
A section view of the tank 114 having the pump 118 at least partially disposed therein is shown in
The pump 118 in the illustrated embodiment has a generally cylindrical shape and includes a pump flange 220 that supports the pump 118 on the mounting flange 216 of the tank 114. An outline view of the pump 118, removed from the tank 114, is also shown in
In the illustrated embodiment, the pushrods 304, shown in cross section in
The pressurized hydraulic fluid to activate the tappet 314 is provided in the space behind the tappet, and is also vented, by the selective positioning of a spool valve 322, which is shown in two operating positions in
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 tappet 314. For example, as shown in
The bore 326 is also fluidly connected to a vent passage 330 (partially shown in
In the illustrated embodiment, the spool valve element 324 at an energized condition is disposed in the fill position (
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
Operation of the actuator 334 depends on the presence of electrical power in the spool 336, which is selectively provided by the electronic controller 120 (
The present disclosure is applicable to any type of application that involves a liquefied gas storage tank. In the illustrated embodiment, a machine having a CNG or LPG fuel source that is carried in an on-board tank was used for illustration, but those of ordinary skill in the art should appreciate that the methods and systems described herein have universal applicability to any type of compressed gas tank that includes a pump for pumping liquefied gas from the tank to supply a system such as an engine with gas.
Two charts that illustrate displacement and supplied liquid flow in a multi-element pump in accordance with the disclosure are shown in
In the illustrated embodiment, the extending speed shown is about 1.25 m/s, while the retracting speed is at about 0.25 m/s, as an exemplary set of operating parameters by which the fill and pumping strokes are carried out at different plunger speeds. These speeds, while they affect the rate at which the liquefied gas is provided to the engine, are also contributing factors to the ability of the pumping elements to seal the pumping volumes for efficient pumping operation, especially for sealing the sliding interface between pump plungers and their respective bores. Moreover, the relatively slower fill strokes promotes efficient fluid retraction into the pumping volume that encloses the pumping plunger.
The pumped, liquefied gas flows resulting from the plunger or tappet displacements shown in
The delay 416 may be selectively set based on various parameters. For example, the dwell time 412 and the second dwell 412′ can contribute to the delay and can be dynamically varied to adjust the delay in real time. For example, for an engine system in which the flows 414 and 414′ represent a fuel supply to the engine, operation at idle or at low load, which requires a low fuelling rate, the delay can be adjusted to ensure that no extra fuel is being pumped to the engine. By the same token, a reduction or elimination in the dwell time 412 can decrease the delay 416. To provide the maximum flow capability, the pump can be designed to have any number of pumping elements, and the stroke length and speed of activation can be selected such that the square waves are adjacent one another providing a zero delay, if desired. It should be appreciated that the pumping elements, because they can be activated independently, can be activated in an overlapping or simultaneous fashion by the controller to further increase the flow rate provided and minimize pressure fluctuations to the engine (i.e., to yield a negative delay 416).
A flowchart for a method of operating a multi-element pump in accordance with the disclosure is shown in
In one embodiment, each pumping stroke may include issuing a command to a hydraulic unit actuator to activate at 510. Activation of the unit actuator may cause a spool valve element to move between a fill position and a vent position at 512, which causes a pushrod to reciprocally displace at 514 and thus activate a plunger or other pumping element at 516 that causes a prearranged flow of fluid to be provided to the engine at 518. The process is repeated during engine operation with changes, as appropriate, to the frequency and dwell time between activations such that a desired flow rate of fluid to the engine is maintained during engine operation. Apart from controlling frequency and duration of pumping element activations, the controller may also control a duration of activation of a pump element such that a shorter pumping stroke may be carried out in the event less than a full stroke of pumped fluid is desired, which is accomplished by a partial plunger displacement.
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.
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.
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