Method and apparatus for pumping a cryogenic fluid from a storage tank

• US 6,640,556 B2
• Filed: 09/19/2001
• Issued: 11/04/2003
• Est. Priority Date: 09/19/2001
• Status: Expired due to Term

• Current Assignee: Westport Fuel Systems Canada Inc. (Westport Fuel Systems, Inc.)
• Original Assignee: Westport Research Inc.
• Inventors: Gram, Anker, Ursan, Mihai
• Primary Examiner(s): Doerrler, William C.
• Assistant Examiner(s): Drake, Malik N.
• Application Number:
  US09/955,825
• Publication Number:
  US 20030051486A1
• Time in Patent Office: 776 Days
• Field of Search: 62/481, 62/501, 62/504, 62/506, 62/507
• US Class Current: 62/50.6
• CPC Class Codes: F04B 15/08 the liquids having low boiling points

Abstract

In the present method and apparatus, cryogenic liquid and vapor are pumped from a storage tank and the proportion of liquid and vapor is controlled so as to influence flow rate through the apparatus. In an induction stroke, the piston of a reciprocating pump is retracted and cryogenic fluid is drawn from the storage tank into a piston chamber associated with the piston. Flow rate is controlled through the apparatus by controlling the proportion of liquid and vapor supplied to the pump during the induction stroke by supplying substantially only vapor to the pump during a portion of the induction stroke. In a compression stroke, the pump compresses and condenses vapor into liquid and then compresses any liquid within the piston chamber; compressed cryogenic fluid is ultimately discharged from the pump. The apparatus preferably includes a pump with a liquid supply line connecting a pump inlet to a storage tank, a vapor supply line connecting an ullage space with a pump inlet, an automatically actuated valve that opens and closes to control the flow of vapor to the pump inlet, and a controller that controls the valve to achieve a desired flow rate.

Claims

1. A method of pumping cryogenic liquid and vapor from a storage tank with a reciprocating piston pump, said method comprising:

(a) in an induction stroke,

retracting a piston disposed within said reciprocating pump and drawing cryogenic fluid from said storage tank into a piston chamber associated with said piston;

controlling flow rate through said pump by controlling the proportion of liquid and vapor supplied to said pump by supplying substantially only vapor during a selected portion of said induction stroke; and

(b) in a compression stroke, compressing and condensing vapor and compressing any liquid within said piston chamber, and discharging compressed cryogenic fluid from said pump.

2. The method of claim 1 wherein for each pump cycle, minimum flow rate pumpable through said pump is determined by the minimum proportion of liquid that is needed during said compression stroke to allow condensation of said vapor within said piston chamber.

3. The method of claim 1 wherein said pump is a single stage pump and for each pump cycle, maximum flow rate pumpable through said pump is achievable by supplying only cryogenic liquid to said pump.

4. The method of claim 1 further comprising condensing vapor supplied from said storage tank in an inducer, and maximum flow rate pumpable through said pump is achievable by supplying a proportion of liquid and vapor to said inducer such that when said inducer completes a compression stroke, said pump piston chamber is substantially filled with liquid.

5. The method of claim 1 wherein flow rate through said pump is controlled to maintain pressure within a predetermined range at a point downstream from said pump.

6. The method of claim 5 further comprising monitoring vapor pressure within said storage tank and further controlling the proportion of vapor and liquid supplied to said pump to maintain vapor pressure within said storage tank below a predetermined value.

7. The method of claim 1 wherein the proportion of liquid and vapor supplied to said pump during said induction stroke is controlled by first supplying liquid until said piston reaches a position during said induction stroke that corresponds to a desired proportion of liquid and then supplying substantially only vapor to fill said piston chamber until said induction stroke is complete.

8. The method of claim 1 wherein cryogenic fluid discharged from said pump is directed to a heater for transforming said cryogenic fluid into a gas.

9. The method of claim 1 wherein said desired proportion of liquid, measured by volume, is constant, such that vapor is supplied to said pump during a predetermined portion of said induction stroke.

10. The method of claim 1 wherein said cryogenic fluid is a combustible fuel and said method further comprises supplying said combustible fuel to an engine.

11. The method of claim 1 wherein the supply of vapor to said piston chamber during said induction stroke is controlled by operating an automatically actuated valve associated with a vapor supply pipe that connects an ullage space of said tank with said pump, said method comprising opening said valve to supply substantially only vapor to said pump and closing said valve to supply substantially only liquid to said pump.

12. The method of claim 11 wherein flow rate through said pump is controlled by controlling when said valve is opened with reference to the position of said piston, and flow rate is increasable by opening said valve for a smaller portion of said induction stroke.

13. The method of claim 12 wherein the position of said pump piston is determined by a sensor that sends an electronic signal to an electronic controller.

14. The method of claim 13 wherein said sensor comprises a linear position transducer associated with said piston.

15. The method of claim 11 wherein said valve is a solenoid valve.

16. The method of claim 15 wherein an electronic controller controls said solenoid valve for achieving a desired pump flow rate while reducing vapor pressure within said storage tank.

17. The method of claim 12 further comprising driving said pump with a linear hydraulic motor.

18. The method of claim 17 wherein the position of said pump piston is determined by monitoring said linear hydraulic motor.

19. The method of claim 17 wherein the position of said pump piston is determined by monitoring a piston rod disposed between said pump piston and said linear hydraulic motor.

20. The method of claim 1 whereby, in addition to controlling flow rate by controlling the proportion of liquid and vapor supplied to said pump, flow rate of said cryogenic fluid may be further controlled by changing pump speed.

21. The method of claim 1 whereby, vapor is supplied to said pump from said storage tank for a fixed portion of said induction stroke and the proportion of liquid and vapor supplied to said pump is controlled by controlling the flow rate of liquid supplied to said pump when vapor is not being supplied from said storage tank.

22. The method of claim 1 whereby, in addition to controlling flow rate by controlling the proportion of liquid and vapor supplied to said pump, flow rate may be further controlled when said pump is a variable displacement pump and displacement is changeable to influence flow rate through said pump.

23. A method of pumping a cryogenic fluid from a storage tank with a reciprocating piston pump, said method comprising:

in an induction stroke,

retracting a piston within said reciprocating pump and drawing cryogenic fluid from said storage tank into a piston chamber associated with said piston;

supplying vapor from said storage tank to said pump through a vapor supply pipe when a valve associated with said vapor supply pipe is open;

supplying cryogenic liquid from said storage tank to said pump through a liquid supply pipe when said valve is closed;

reducing vapor pressure within said storage tank and controlling pump flow rate by controlling the timing for opening said valve during said induction stroke; and

(b) in a compression stroke,

reversing the direction of said piston to compress and condense vapor and compress the cryogenic liquid within said piston chamber; and

discharging compressed cryogenic fluid from said pump.

24. The method of claim 23 wherein said pump draws substantially only cryogenic liquid into said piston chamber when said valve is closed and draws substantially only vapor when said valve is open.

25. The method of claim 23 wherein timing for opening said valve is determined by a controller with reference to pressure measured at a point downstream from said pump to which said compressed cryogenic fluid is directed.

26. An apparatus for pumping a cryogenic fluid from a storage tank and reducing vapor pressure within said storage tank, said apparatus comprising:

(a) a reciprocating pump for pumping said cryogenic fluid supplied from said storage tank;

(b) a liquid supply pipe that fluidly connects said storage tank to an inlet of said pump;

(c) a vapor supply pipe that fluidly connects an ullage space within said storage tank to said inlet;

(d) an automatically actuated valve associated with said vapor supply pipe, said valve being operable between a closed and an open position for allowing vapor to flow through said vapor supply pipe when said valve is in said open position;

(e) a controller for determining when to open said valve during an induction stroke of said pump, said controller making such determination to achieve a desired flow rate; and

(f) a position sensor for determining the position of a piston of said pump, said position sensor in communication with said controller so that said controller opens said valve when said piston is in a position to corresponds to the desired proportion of liquid for said induction stroke.

27. The apparatus of claim 26 wherein said position sensor comprises a linear position transducer associated with said piston.

28. The apparatus of claim 26 wherein said valve is a solenoid valve.

29. The apparatus of claim 26 further comprising a linear hydraulic motor for driving said pump.

30. The apparatus of claim 26 further comprising an accumulator vessel that is fluidly connected to a discharge port of said pump.

31. The apparatus of claim 30 wherein said cryogenic fluid is a combustible fuel.

32. The apparatus of claim 31 further comprising a heater for heating cryogenic fluid discharged from said pump.

33. The apparatus of claim 26 further comprising an internal combustion engine that is fluidly connected to a discharge port of said pump, and said combustible fuel is usable as fuel for said engine.

34. The apparatus of claim 26 wherein said reciprocating pump is a single acting pump comprising a single piston reciprocable within a single piston chamber.

35. An apparatus for pumping a cryogenic fluid from a storage tank and reducing vapor pressure within said storage tank, said apparatus comprising:

(a) a reciprocating pump for pumping said cryogenic fluid supplied from said storage tank;

(b) a liquid supply pipe that fluidly connects said storage tank to an inlet of said pump;

(c) a vapor supply pipe that fluidly connects an ullage space within said storage tank to said inlet;

(d) an automatically actuated valve associated with said vapor supply pipe, said valve being operable between a closed and an open position for allowing vapor to flow through said vapor supply pipe when said valve is in said open position;

(e) a controller for determining when to open said valve during an induction stroke of said pump, said controller making such determination to achieve a desired flow rate; and

(f) an inducer, which is fluidly disposed between said storage tank and said reciprocating pump, said inducer comprising an inlet for receiving cryogenic fluid from said storage tank, an inducer piston that is reciprocable within an inducer piston chamber for compressing and condensing cryogenic vapor and compressing cryogenic liquid; and

said pump comprising an inlet for receiving compressed cryogenic fluid from said inducer, and a pump piston that is reciprocable within a pump piston chamber for further compressing said cryogenic fluid.

36. The apparatus of claim 35 further comprising a one-way flow conduit for transferring cryogenic fluid from said inducer piston chamber to said pump piston chamber.

37. The apparatus of claim 35 wherein when said pump piston chamber is filled with cryogenic fluid transferred from said inducer piston chamber, excess cryogenic fluid is recyclable within said inducer.

38. The apparatus of claim 35 wherein said inducer piston chamber is volumetrically larger than said pump piston chamber.

39. The apparatus of claim 38 wherein said inducer piston chamber has a volume that is at least two times larger than the volume of said pump piston chamber.

40. The apparatus of claim 38 wherein said inducer piston chamber has a volume that is between about four and seven times larger than the volume of said pump piston chamber.

41. The apparatus of claim 35 further comprising a linear hydraulic motor that drives both said inducer piston and said pump piston.

42. The apparatus of claim 40 further comprising a piston rod connecting said hydraulic motor with said inducer piston and said pump piston.

43. The apparatus of claim 35 wherein said inducer piston divides said inducer piston chamber into a first stage in communication with said inducer inlet and a second stage in communication with said pump piston chamber and a one-way flow conduit allows cryogenic fluid to flow from said first stage to said second stage, another one-way flow conduit allows cryogenic fluid to flow from said second stage to said pump piston chamber, and a pressure actuated valve allows cryogenic fluid to flow from said second stage to said first stage when pressure within said second stage exceeds a predetermined value.