This invention relates generally to a fuel transfer pump system and, in particular, to a pulse width modulated (PWM) fuel transfer pump system comprising a multi-mode control process for delivering fuel to, for example, a high pressure fuel injection pump. In turn, and in one embodiment, the high pressure fuel injection pump delivers high pressure fuel to a common rail system in fluid communication with fuel injectors that deliver fuel to individual engine cylinders under the control of an electronic or engine control unit (ECU).
Diesel Engines in the 900 to 6,600 HP range typically have fuel injection pumps capable of pressurizing fuel up to and over 30,000 psi. Historically, a fuel injection pump has been placed with an injector on each cylinder. Today, most manufacturers have switched to a single fuel injection pump and a high pressure accumulator, known as a “Common Rail.” In most applications, the fuel injection pump must be fed by a fuel transfer pump. The fuel transfer pump provides fuel to the fuel injection pump at a sufficient flow rate and pressure to allow for successful operation.
Historically, mechanically driven fuel transfer pumps have been the predominant method of fuel transfer, but not without problems.
For example, a typical mechanically driven fuel transfer pump normally has a dynamic shaft seal which prevents fuel from escaping into the engine or into the environment. This seal can become damaged by wear or debris and leak—creating a safety, reliability, and/or maintenance point.
Additionally, the mechanically driven fuel transfer pump RPM is directly tied to engine speed; however, fuel consumption is not always directly proportional to engine speed and, as a result, the pump must be sized for all possible combinations of fuel consumption and RPM. As a result, the pump provides much more flow than is needed most of the time. Accordingly, this extra flow normally is drained back to the fuel tank and the power required to pump the fuel up to pressure is lost thereby wasting energy.
A further problem with the mechanically driven fuel transfer pump RPM is that when the engine is cranking or idling (lowest RPM) the pump may not have enough lift capability to lift fuel from the main fuel tank to the fuel injection pump. This problem is made worse when the fuel tank is positioned significantly lower than the pump, as in locomotives, where the pump normally has to lift fuel at least 6 feet. This can prevent successful priming and keep fuel from reaching the fuel injection pump. To counter this problem, many manufacturers install a third priming pump that is either hand operated or electric motor driven for lifting fuel from the tank to the fuel transfer pump to prime it before cranking the engine. This creates added cost and complexity.
Today, electric motor driven fuel transfer pumps are an addition to the mechanically driven fuel transfer pumps and take the form of either a DC motor driven fuel transfer pump or an AC motor driven fuel transfer pump.
The DC motor driven fuel transfer pumps are problematic for a variety of reasons. First, a category of DC motor driven fuel transfer pumps utilize a dynamic shaft seal that is similar to the seal used in the mechanical version noted above thereby resulting in the same problem of the seal becoming damaged by wear or debris and resulting in a leak creating a safety, reliability, and/or maintenance point. Another problem associated with the DC motor driven fuel transfer pump is motor brush life. In applications such as locomotives, the pump is expected to operate for up to 10 years of continuous duty. This type of duty cycle results in numerous brush changes thereby increasing maintenance costs and chance of failure.
Current AC motor driven fuel transfer pumps operating in applications where only DC power is available accomplish this through a power inverter that creates an AC output from DC input to drive the AC motor.
The inverter for these pumps operates open loop, which means the controller drives the motor at a maximum RPM when maximum voltage is available. RPM can be slowed by lowering available voltage, but this is not practical when other components on the machine are dependent upon the full voltage. Fuel pressure is regulated by mechanical valves. In this case, as in all examples listed above, the pump is sized for maximum fuel consumption. In normal operation, when maximum fuel is not consumed, the fuel is bypassed back to the tank. This adds heat to the fuel and consumes more electrical power than what is actually required to deliver the necessary fuel and wears pump components faster than necessary. Furthermore, pumping excess fuel drives excessive filter sizing and expense.
For the foregoing reasons, there is a need for a fuel transfer pump that, inter alia, overcomes the significant shortcomings of the known prior-art as delineated hereinabove.
BRIEF SUMMARY OF THE INVENTION
In general, and in one aspect, an embodiment of the invention provides a pulse width modulated (PWM) fuel transfer pump system comprising a multi-mode control process for efficiently delivering fuel to a high pressure fuel injection pump under multiple modes of system and engine operation.
In another aspect, an embodiment of the invention provides a fuel transfer pump system that is a cost effective energy management system that operates on demand and under multiple modes of system and engine operation. Thus, there is a cost savings versus using prior conventional mechanically and electric motor driven fuel transfer pumps.
In another aspect, an embodiment of the invention provides a fuel transfer pump system that comprises an AC Induction motor and a multi-mode control process which dynamically controls the speed of the AC induction motor for delivering a target pressure of fuel to the high pressure fuel injection pump over a broad range of engine operating conditions. Hence, the fuel transfer pump system dynamically controls the delivery of fuel to the high pressure fuel injection pump as opposed to the static delivery of fuel by the prior conventional mechanically and electric motor driven fuel transfer pumps. Accordingly, this control can result in a reduction in filter size and/or extending filter life.
In another aspect, an embodiment of the multi-mode control process of the fuel transfer pump system dynamically switches between multiple modes of control as a function of engine start up, running, and shut down conditions and also as a function of anomalous conditions of operation.
In another aspect, an embodiment of the multi-mode control process of the fuel transfer pump system dynamically compensates for voltage fluctuations of the power source powering the system.
In another aspect, an embodiment of the invention provides a method for controlling a fuel transfer pump delivering fuel to a high pressure fuel injection pump; the method comprising: providing a fuel transfer pump having an inlet port which is connectable in fluid communication with a fuel source and an outlet port which is connectable in fluid communication with a high pressure fuel injection pump; providing a motor for driving the fuel transfer pump for drawing fuel through the inlet port from the fuel source and pumping pressurized fuel out the outlet port; measuring a fuel pressure at a location which is in fluid communication with the outlet port; controlling an operating speed of the motor driving the fuel transfer pump as a function of the measured fuel pressure for defining a closed loop pressure control mode for controlling the measured fuel pressure to a target fuel pressure; measuring a current utilized in operating the motor; comparing the measured current to a predefined threshold current value; correlating the measured current to at least one anomalous condition when indicated by the comparison step; and switching from the closed loop pressure control mode for controlling the operating speed of the motor as a function of the measured fuel pressure to a current control mode for controlling the operating speed of the motor as a function of the measured current when the measured current is correlated by the correlation step to at least the one anomalous condition.
In another aspect, an embodiment of the invention provides a method for minimizing current inrush to a fuel transfer pump upon start up; the method comprising: providing a fuel transfer pump having an inlet port which is connectable in fluid communication with a fuel source and an outlet port which is connectable in fluid communication with a high pressure fuel injection pump; providing a motor for driving the fuel transfer pump for drawing fuel through the inlet port from the fuel source and pumping pressurized fuel out the outlet port; measuring a fuel pressure at a location which is in fluid communication with the outlet port; controlling an operating speed of the motor driving the fuel transfer pump as a function of the measured fuel pressure and a moving fuel pressure; measuring a current utilized in operating the motor; comparing the measured current to a predefined threshold current value; and ramping up the current utilized in operating the motor when the measured current is below the predefined threshold current value as indicated by the comparison step and ramping down the current utilized in operating the motor when the current is above the predefined threshold current value as indicated by the comparison step for providing the moving fuel pressure until the moving fuel pressure reaches a target fuel pressure.
In another aspect, an embodiment of the invention provides a fuel transfer pump system for delivering fuel to a high pressure pump of a fuel injection system, the fuel transfer pump system comprising: a fuel transfer pump having an inlet port which is connectable in fluid communication with a source of fuel and an outlet port which is connectable in fluid communication with a high pressure fuel injection pump; a motor for driving the fuel transfer pump for drawing fuel through the inlet port from the fuel source and pumping pressurized fuel out the outlet port at a target fuel pressure; means for measuring fuel pressure at a location in fluid communication with the outlet port of the fuel transfer pump; means for measuring current utilized in operating the motor; and a controller operatively coupled to the motor and connected in signal communication with the fuel pressure measuring means and the current measuring means, the controller being configured to adaptively switch between a closed loop pressure control mode for controlling an operating speed of the motor for obtaining the target fuel pressure as a function of the measured fuel pressure to a current control mode for controlling the operating speed of the motor as a function of the measured current when the measured current is correlated to at least one anomalous condition based on a comparison between the measured current and a predefined threshold current value.
In a further aspect, an embodiment of the invention provides a non-transitory microcontroller-readable memory containing microcontroller-executable instructions that, when executed by a processor, cause the processor to perform a multi-mode control method of a motor driving a pump, the method comprising: controlling an operating speed of a motor driving a pump for pressurizing fluid as a function of a measured pressure of the pressurized fluid for defining a closed loop pressure control mode for obtaining a target fluid pressure; and switching from the closed loop pressure control mode to a current control mode for controlling the operating speed of the motor as a function of a measured current utilized in operating the motor when the measured current is indicative of at least one anomalous condition.
Accordingly, it should be apparent that numerous modifications and adaptations may be resorted to without departing from the scope and fair meaning of the claims as set forth herein below following the detailed description of the invention.
Considering the drawings, wherein like reference numerals denote like parts throughout the various drawing figures, reference numeral 10 is directed to a fuel transfer pump system: apparatus and method.
System Overview
In general, and referring to
Additionally, fuel transfer pump system 10 is comprised of a pressure transducer 36 located downstream from the fuel transfer pumnp 14 for measuring the inlet fuel pressure to the high pressure pump 26 for use as will be delineated in detail below. In one embodiment, the pressure transducer 36 is disposed in the second fuel line before the stage-two fuel filter 24. In another embodiment, the pressure transducer 36 is disposed in the second fuel line after the stage-two fuel filter 24. Furthermore, the fuel transfer pump system 10 is comprised of a fuel temperature sensing means 38 located downstream from the fuel tank 20 for measuring the inlet fuel temperature to the fuel transfer pump 14 for use as will be delineated in detail below.
PWM Inverter System
Referring to
Additionally, the PWM inverter system 18 is comprised of a DC bus voltage sensing means 52, a DC bus current transducer means 54, a first or phase-A current transducer means 56, and a second or phase-B current transducer means 58. The DC bus voltage sensing means 52 and a DC bus current transducer means 54 are both electrically coupled between the DC bus 48 and the Microcontroller 40. The first or phase-A current transducer means 56 and the second or phase-B current transducer means 58 are both electrically coupled between the AC motor 16 and the Microcontroller 40. The PWM inverter system 18 is also comprised of a power transistor temperature sensing means 60, a microcontroller (MCU) temperature sensing means 62, and a CANBUS means 64. The power transistor temperature sensing means 60 is electrically coupled between the three phase inverter bridge circuit 42 and the Microcontroller 40, the microcontroller temperature sensing means 62 is electrically coupled to the Microcontroller 40, and the CANBUS means 64 is electrically coupled between the Microcontroller 40 and the ECU 34 for providing bidirectional communication between the two. Both the pressure transducer 36 and the fuel temperature sensing means 38 are also electrically coupled to the Microcontroller 40.
Furthermore, and referring to
Moreover, the Microcontroller 40 is comprised PWM up/down counter 202, a digital signal processor 204, a RAM 206, a data memory 208 which, in one embodiment, is in a form of a EEPROM, and a program memory 210 all of which will be further detailed below.
Schematically Depicted PWM Inverter System
More specifically, one embodiment of the PWM inverter system or controller 18 is schematically depicted in
Multi Mode Control Process/Method
Referring back to
The multi-mode control process 222 is comprised of coded instructions that are stored in a program memory 210 of the Microcontroller 40 and that are illustrated in flowchart form in
Outer Lower Priority Loop Process
Referring to
At the outset, the outer loop process 224 begins with a power on signal 226 initiated by, for example, starting of the engine 32 or perhaps by an engine prestart condition that actuates power on signal 226. Next, the process 224 flows to process block 228 for initializing initializes variables and setting up communication, A/D, and pulse width modulated peripherals. Then, process block starts an A/D conversion 234 via A/D converter 192 (
Then, the outer loop 224 proceeds to decision block 240 for determining if a run pump command has been given and, if yes, the process flow proceeds to decision block 242 for determining if the pump 14 is running and if yes, the pump is running, then the outer loop process 224 loops back to process block 236 and process flow continues. If no, the pump is not running, then the process flows to process block 244 for charging high side boot strap capacitors delineated above and shown in
Alternatively, if the result of decision block 240 is no, then the process flows to decision block 248 for determining if the pump 14 is running and if no, the pump is not running, then the outer loop process 224 loops back to process block 236 and process flow continues. If yes, the pump is running, then the process flows to decision block 250 for determining if the multi-mode control process 222 is in a pressure control mode 272 and if yes, then at process block 252 the pressure control mode 272 (
A/D Conversion-Complete Interrupt Process
At the outset, the initial PWM period counter process starts with decision block 230 for determining if a PWM up/down counter 202 (
Upon completion of the A/D conversion process 234, the A/D conversion complete interrupt process 260 begins at block 262 and proceeds to process block 264 for running a transform and average measurement process 416 detailed below and in
Next, the process proceeds to decision block 266 for determining if a run pump command has been given and, if no, then the process proceeds to exit the A/D conversion interrupt at block 268 and return to the outer lower priority control loop process 224 which resumes where it left off. If the result of decision block 266 is yes, then the process proceeds to decision block 270 for determining if the multi-mode control process 222 is in the pressure control mode 272 and, if no, then the process proceeds to process block 272 wherein the process enters ramp-down mode 302 utilizing the open loop RPM control 212 and, if the result is yes, then the process proceeds to a RPM control process 274 detailed below and in
Next, the process proceeds to process block 276 for calculating a open loop angular position from the commanded RPM for determining how much angle does the rotor of the motor 16 need to traverse for a given amount of time (Δt) to achieve the commanded RPM. The RPM multiplied by At equals the angle and the time is fixed and determined by the carrier frequency of the system 10.
Still referring to
Then, process 260 proceeds to exit the A/D conversion interrupt at block 268 and the outer lower priority control loop process 224 resumes where it left off.
RPM Control Process
Referring to
Alternatively, if the result of the decision block 276 is no, then a current limit flag is set to false at process blck 286. Then a decision is made at decision block 288 for determining if the DC bus voltage, VDC in
Then, process flow is then passed to the above noted decision block 300 for determining if the pump is in the soft start mode 304. If the result of decision block 300 is yes, then the process flows to decision block 312 for determining if the pressure setting (the instantaneous pressure that the pump maintains) is greater than or equal to the target pressure (the pressure that the pump is desired to achieve or controlled to). If the result of decision block 312 is yes, then process block 314 makes a determination that the soft start mode 304 is complete and ends the soft start mode of operation of the motor 16 and, if the result of decision block 312 is no, then the pressure setting is raised by a predetermined amount which, in one embodiment, is two psi. After either process block 314 or 316, or if the result of decision block 300 is no, the process flow is to a decision block 318 in
Referring now to
Alternatively, if the result of decision block 320 is no, then the process flows to decision block 324 for determining if the pressure setting (the instantaneous pressure that the pump maintains) is greater than the target pressure (the pressure that the pump is desired to achieve). If the result of decision block 324 is yes, then at process block 326 the pressure setting is decreased by a predetermined amount which, in one embodiment, is two psi and then the process flows to the above noted decision block 328. If the result of decision block 324 is no, then the process flows to the above noted decision block 328.
With the pressure setting increased, decreased, or unchanged, decision block 328 determines if the pressure measured from the pressure transducer 36 is less than the predetermined amount and if the DC bus current is greater than the predetermined amount. If the result of decision block 328 is yes, then the multi-mode control process 222 enters the current control mode 282 (Mode 2 ) and a Stage II clogged filter flag is set to true and a status flag may be sent to the ECU for causing an actuation of a visual and/or audio indication 334 (
With the RPM calculated from the current control PID process 364, the process flows to process block 342 for calculating a PWM duty utilizing the Volts/Hertz Curve or profile 214 detailed below and in
Alternatively if the results of decision block 328 is no, then a subsequent decision is made at decision block 336 for determining if the pressure measurements, current measurements, and RPMs are correlative to calculated or empirically determined values that are representative of a clogged Stage I filter. If the result of decision block 336 is yes, then a Stage I clogged filter flag is set to true and the visual and/or audio indication 334 (
Process block 340 utilizes the pressure control PID process 390 detailed in
Now, if the result of decision block 318 is no, then the process flows to decision block 344 for determining if the pressure measured by the pressure transducer is greater than a predefined threshold which, in one embodiment, is 90 psi. If the result of decision block 344 is no, then the process flows to process block 332 and 342 which have been delineated in detail above and the RPM control process 274 ends after process block 342.
Alternatively if the result of decision block 344 is yes, then the process flows to process block 346 for returning the multi-mode control process 222 to the pressure control mode 272 (Mode 1) and setting the Stage II clogged filter flag to false. From process block 346, the process flows to decision block 328 from which the process flows as delineated in detail above until ending after process block 342.
Thermal Protection Process
Referring back up to decision block 346, if the answer to decision block 346 is yes, then the process flows to decision block 354 for determining if a hot-start timer is on and, if the answer to decision block 354 is yes, then the process flow is to decision block 358 for determining if the hot-start timer has expired and, if the answer to decision block 354 is no, the process flow is first to a process block 356 for starting the hot-start timer and then to decision block 358. Decision block 358 determines if the hot start timer has expired and, if no, then the tliermal protection process 344 ends and, if yes, then the process flows to decision block 360 for determining if the fuel temperature 198, the MOSFET temperature 194, and the Microcontroller temperature 196 are all below predetermined allowed maximums. If the answer to decision block 360 is yes, then the process flows to process block 362 for setting the hot-start flag to false wherein the hot- start flag can only be reset by cycling power and wherein setting the hot-start flag to false is followed by the end of the thermal protection process 344. Alternatively, if the answer to decision block 360 is no, then the process flows to process block 350 followed by process block 352 which, in turn, is followed by the end of the thermal protection process 344 as delineated above.
Current Control PID Process
The current control PID process 364 commences with process block 366 for calculating an error which is the DC bus current target (e.g., 40 amps) minus the DC bus current measurement (IDC). Then the process 364 flows to process block 368 for determining a delta error or difference which is equal to the error minus the last error calculated. Next, the process flows to process block 370 for calculating an output that is equal to the last output stored plus a predefined proportional coefficient times the current error plus a predefined derivative coefficient times a delta error divided by a delta time where delta time is constant because the system 10 is utilizing a fixed frequency. Then the process flows to process block 372 for storing the output calculated in process block 370 as Output Temp.
Next, the process flows to decision block 374 for determining if the output is greater than a predefined output maximum and if yes, then output is defined as the output maximum at process block 376. If no, decision block 378 determines if the output is less than a predefined output minimum. If the result of decision block 378 is yes, then the output is defined as the output minimum at process block 380 and, if no, then the output is defined at process block 382 as the previously stored output in process block 372. Then, one of these three outputs is passed to process block 384 for defining the RPM Out. Next, error is accumulated at process block 386 by setting the output to the Output Temp value plus a predefined integral coefficient times the value obtained by taking the difference between the error and the Output Temp value minus the output value. Finally, process block 388 stores the error obtained at process block 386 as the last error and the current control PID process 364 ends.
Pressure Control PID Process
The pressure control PID process 390 commences with process block 392 for calculating an error which is the pressure target (e.g., 110 psi) minus the pressure measurement 200. Then the process flows to process block 394 for determining a delta error or difference which is equal to the error minus the last error calculated. Next, the process flows to process block 396 for calculating an output that is equal to the last output stored plus a predefined proportional coefficient times the current error plus a predefined derivative coefficient times a delta error divided by a delta time where delta time is constant because the system 10 is utilizing a fixed frequency. Then the process flows to process block 398 for storing the output calculated in process 396 as Output Temp.
Next, the process flows to decision block 400 for determining if the output is greater than a predefined output maximum and if yes, then output is defined as the output maximum at process block 402. If no, decision block 404 determines if the output is less than a predefined output minimum. If the result of decision block 404 is yes, then the output is defined as the output minimum at process block 406 and, if no, then the output is defined at process block 408 as the previously stored output in process block 398. Then, one of these three outputs is passed to process block 410 for defining the RPM Out. Next, error is accumulated at process block 412 by setting the output to the Output Temp value plus a predefined integral coefficient times the value obtained by taking the difference between the error and the Output Temp value minus the output value. Finally, process block 414 stores the error obtained at block 412 as the last error and the pressure control PID process 390 ends.
Transform and Average Measurements Process
After process block 420, the process flows to decision block 422 for determining if the pressure transducer 36 has failed high or low and, if yes, then continues to process block 424 for setting a pressure failure flag to true followed by continuing to process block 426 for setting the motor run flag to false and then to decision block 428. Alternatively, if the answer to decision block 422 is no, then the process proceeds directly to decision block 428. Decision block 428 determines if the case number is less than four and, if yes, the index (i) is incremented by one at process block 430 which is followed by process block 432 multiplexed to read channel (i) or, in other words the next channel so that the next case will be read on the next cycle of the transform and average measurement process 416. Process block 432 is followed by the end of one cycle of the transform and average measurement process 416.
Alternatively, if the result of decision block 428 is no, then the process flow is to process block 434 for resetting (i) to zero as a result of (i) being incremented by 1 for each cycle from zero to four wherein on the first cycle (i)=3, on the second cycle (i)=1, on the third cycle (i)=2, on the fourth cycle (i)=3, and on the fifth cycle (i)=4 and is then reset to zero. Thus, the transform and average measurement process 416 is performed on cases zero through four. After process block 434, the process flow is to process block 432 followed by the end of one cycle of the transform and average measurement process 416 as delineated above.
Calculate PWM Duty From Volts/Hertz Curve Process
DC Bus Voltage Compensation PID Control Process
The DC bus Voltage Compensation PID control process 438 commences with process block 440 for calculating an error which is the maximum allowed RPM for a given DC bus voltage minus the commanded RPM. Then the process flows to process block 442 for determining a delta error or difference which is equal to the error minus the last error calculated. Next, the process flows to process block 444 for calculating an output that is equal to the last output stored plus a predefined proportional coefficient times the current error plus a predefined derivative coefficient times a delta error divided by a delta time where delta time is constant because the system 10 is utilizing a fixed frequency. Then the process flows to process block 446 for storing the output calculated in process block 444 as Output Temp. Next, the process flows to decision block 448 for determining if the output is greater than a predefined output maximum and if yes, then output is defined as the output maximum at process block 450. If no, decision block 452 determines if the output is less than a predefined output minimum. If the result of decision block 452 is yes, then the output is defined as the output minimum at process block 454 and, if no, then the output is defined at process block 456 as the previously stored output in process block 446. Then, one of these three outputs is passed to process block 458 for defining the Pressure target or target pressure. Next, error is accumulated at process block 460 by setting the output to the Output Temp value plus a predefined integral coefficient times the value obtained by taking the difference between the error and the Output Temp value minus the output value. Finally, process block 462 stores the error obtained at block 460 as the last error and the DC bus Voltage Compensation PID control process 438 ends.
Fuel Transfer Pump Apparatus Configuration
The fuel transfer pump system 10 can be packaged as one or more individual pieces or in a form of, but not limited to, a one piece motor-pump-control assembly as depicted by fuel transfer pump 510 illustrated in
Referring now to
In one embodiment, the fuel circulates through passages in the motor housing 512 for providing cooling and the controller 18 is mounted to the pump body 518 and relies on the fuel for heat removal.
In Use and Operation
In use and operation, and referring to the drawings, one embodiment of the fuel transfer pump system 10 is utilized on medium and large horsepower diesel engines. The fuel transfer pump system 10 delivers fuel from the fuel tank 20 to the high pressure fuel injection pump at, but not limited to, about 0 to about 120 psi, with a variable flow rate from about 0 to about 12 gallons per minute. Input voltage to the system 10 is either, but not limited to, 24 or 74 volts DC. The fuel transfer pump 14 is, but not limited to, an external gear pump, driven by the AC induction motor 16. Varies motor sizes such as a one-half or a three-quarter horsepower motor serve as size examples of the AC induction motor 16. In particular, a stator and a rotor for the one-half horsepower motor are supplied BALDOR under rerspective parts numbers 34L481S546G1S and 34L482S546G1R.
Additionally, and in use and operation, the fuel transfer pump system 10 comprises the multi-mode control process 222 which, in one embodiment, is comprised of the pressure control mode 272 (Mode 1) including soft start up mode 304; the current control mode 282 (Mode 2); the DC-bus voltage compensation mode 292 (Mode 3); and the open loop ramp down mode 302 (Mode 4) for ramping open loop motor RPMs to zero from any of the other control modes of operation.
The pressure control mode 272 (Mode 1) is a closed loop pressure control mode for maintaining the fuel pressure at the outlet of the fuel transfer pump 14 at a substantially constant target pressure. The fuel transfer pump system 10 maintains the target pressure at the high pressure fuel injection pump 26 inlet by varying the RPM of AC motor 16 which, in turn varies the RPM of the pump 14 for varying the fuel flow rate for maintaining the target pressure. The feedback information about outlet fuel pressure is provided by the pressure transducer 36 which is utilized by the pressure control PID process 390 for reiteratively calculating the difference (error) between the target pressure (pressure that is to be maintained substantially constant) and the measured pressured and transforming this difference into a commanded RPM that is provided to the open loop RPM control means 212 for controlling the AC motor 16 for driving the pump 14 for controlling the flow rate of fuel for obtaining the target pressure.
At start up, the fuel transfer pump system 10 utilizes the soft start mode 304 to minimize current inrush during the initial motor start up and also to eliminate voltage sag on the power source 12. The soft start mode 304 provides the means for bidirectionally ramping up to the target pressure by utilizing a soft start profile 306 in combination with the closed loop pressure control mode 272. The soft start profile 306 is illustrated in
Referring now to
Hence, in current control mode 282, the system 10 deliveries as much fuel as it can without exceeding a predetermined maximum current level. Accordingly, the system 10 can delivery fuel flow but at a level below target pressure so that the engine can run, but not at full power. In one scenario, the pressure transducer is operating, but senses a flow restriction. Thus, if the system 10 is measuring DC bus current that is greater than the predetermined maximum, and the pressure is below target pressure, then the system goes into current control mode 282 to safely deliver fuel pressure without exceeding the predetermined maximum current level.
The DC bus Voltage Compensation control mode 292 (Mode 3) solves the problem of having a difference or sag between a DC design voltage and the actual DC voltage provided by the power source 12. For example, if the designed voltage is 24 volts at 3600 RPM, then if the power source voltage is actually 20 volts the system 10 cannot be run at 3600 RPM, but be at a point on the Volts/Hertz profile or curve 214 (
Referring back to
During start up, the target pressure obtained from the DC Bus Voltage Compensation HD Control process 438 is utilized by the soft start mode 304 for bidirectionally ramping up a moving target pressure to the target pressure associated with the measured DC bus voltage.
Hence, the DC bus Voltage Compensation control mode 292 (Mode 3) adjusts the maximum available RPM as a function of DC bus voltage fluctuations for protecting the AC motor from excessive current and for protecting the AC motor and the associated electronics from overheating. Additionally, the DC bus Voltage Compensation control mode 292 (Mode 3) is employed in combination with the current control mode 282 (Mode 2) to assure that a target pressure associated with a sag in DC Bus voltage is not exceeded.
Accordingly, when the system 10 is in Mode 3, it is also in Modes 1 or 2 or, in other words, Mode 3 is a parent of Mode 1 or 2 when Mode 3 is active.
The open loop ramp down mode 302 (Mode 4) utilizes the open loop rpm control 212 (
Accordingly, it should be apparent that further numerous modifications and adaptations may be resorted to without departing from the scope and fair meaning of the present invention as set forth hereinabove and as described herein below by the claims.
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