Process and apparatus for conditioning cryogenic fuel to establish a selected equilibrium pressure

• US 5,590,535 A
• Filed: 11/13/1995
• Issued: 01/07/1997
• Est. Priority Date: 11/13/1995
• Status: Expired due to Term

• Current Assignee: Chicago Bridge & Iron Company (Mcdermott International Incorporated)
• Original Assignee: Chicago Bridge & Iron Technical Services Company
• Inventors: Rhoades, George D.
• Primary Examiner(s): Capossela, Ronald C.
• Application Number:
  US08/557,992
• Time in Patent Office: 421 Days
• Field of Search: 62/50.2, 62/7, 62/657
• US Class Current: 62/50.2
• CPC Class Codes: F17C 2221/012 Hydrogen
• CPC Class Codes: F17C 2221/033 Methane, e.g. natural gas, CNG, LNG, GNL, GNC, PLNG
• CPC Class Codes: F17C 2223/0161 cryogenic, e.g. LNG, GNL, PLNG
• CPC Class Codes: F17C 2223/033 Small pressure, e.g. for liquefied gas
• CPC Class Codes: F17C 2227/0306 using the same fluid
• CPC Class Codes: F17C 2227/0339 using the same fluid
• CPC Class Codes: F17C 2250/01 Intermediate tanks
• CPC Class Codes: F17C 2250/0439 Temperature
• CPC Class Codes: F17C 2250/0626 Pressure
• CPC Class Codes: F17C 2250/0631 Temperature
• CPC Class Codes: F17C 2265/065 for refueling vehicle fuel tanks
• CPC Class Codes: F17C 2270/0168 by vehicles
• CPC Class Codes: F17C 9/02 with change of state, e.g. vaporisation
• CPC Class Codes: Y02E 60/32 Hydrogen storage

Abstract

A method and apparatus for conditioning cryogenic fuel includes providing a primary storage tank for liquefied cryogenic fuel, a vapor storage tank communicating with the primary storage tank for storing vapor withdrawn from the primary storage tank at a higher pressure than the pressure in the primary storage tank, and a conditioning system wherein heat is transferred to the colder, lower equilibrium pressure liquefied cryogenic fuel withdrawn from the primary storage tank. The conditioning system includes a heat exchanger system for transferring heat to the liquefied cryogenic fuel from vapor withdrawn from the vapor storage tank. The vapor is cooled to near saturation temperature in the heat exchanger and is then sparged into liquefied cryogenic fuel flowing through a sparger or mixer chamber disposed downstream of the heat exchanger. A temperature sensor disposed in a conduit downstream of the sparger or mixer chamber measures the temperature (and thus the equilibrium pressure) of the warmed cryogenic fuel in the conduit. A temperature controller in communication with the temperature sensor regulates the flow rate of vapor from the vapor storage tank to the cryogenic fuel conditioning system in response to a signal from the temperature sensor.

Claims

1. A method of conditioning cryogenic fuel comprising the steps of:

(a) withdrawing liquefied cryogenic fuel from a primary storage tank at a low pressure and at a temperature close to the boiling point of the liquefied cryogenic fuel;

(b) warming the liquefied cryogenic fuel by feeding the fuel through means for warming the fuel;

(c) withdrawing vapor from a vapor space in the primary storage tank and feeding the vapor to a vapor storage tank at a selected pressure higher than the pressure in the primary storage tank;

(d) feeding the vapor from the vapor storage tank to the means for warming the liquefied cryogenic fuel wherein heat is indirectly transferred from the vapor to the liquefied cryogenic fuel and the vapor is subsequently condensed;

(e) subsequently feeding the liquefied cryogenic fuel through means for dispensing the liquefied cryogenic fuel into a vehicle fuel tank;

(f) measuring a temperature of the cryogenic fuel in the dispensing means; and

(g) providing the cryogenic fuel to the vehicle fuel tank at a selected equilibrium pressure by varying a flow rate of the vapor withdrawn from the vapor storage tank and fed into the means for warming the liquefied cryogenic fuel in response to the temperature of the liquefied cryogenic fuel in the dispensing means.

2. The method of claim 1 wherein the vapor withdrawn from the primary storage tank is fed through a compressor to increase the pressure thereof prior to being fed into the vapor storage tank.

3. The method of claim 1 wherein the step of warming the liquefied cryogenic fuel further comprises the steps of:

(a) feeding the liquefied cryogenic fuel through a heat exchanger wherein the vapor from the vapor storage tank is also fed through the heat exchanger and is cooled to near a saturation temperature thereof; and

(b) combining the vapor exiting the heat exchanger with the liquefied cryogenic fuel exiting the heat exchanger.

4. The method of claim 3 wherein the vapor exiting the heat exchanger is blended into the liquefied cryogenic fuel exiting the heat exchanger.

5. The method of claim 1 wherein the step of measuring the temperature of the liquefied cryogenic fuel is performed with a temperature sensor which communicates a signal indicative of equilibrium temperature and pressure to a controller and including the step of determining with the controller, in response to the signal from the temperature sensor, a flow rate of the vapor into the means for warming the liquefied cryogenic fuel.

6. The method of claim 5 further comprising providing a monitor communicating with the temperature sensor, said monitor comprising a temperature indicator and a manual override of the controller.

7. The method of claim 6 wherein said temperature indicator comprises a readout for an equivalent equilibrium pressure.

8. The method of claim 1 further comprising the step of reducing an internal pressure of a vehicle fuel tank by allowing fuel to flow from the vehicle fuel tank to the primary insulated storage tank.

9. The method of claim 1 further comprising the step of removing liquefied cryogenic fuel from a vehicle fuel tank by flowing vapor directly from the vapor storage tank directly into the vehicle fuel tank.

10. A method of conditioning cryogenic fuel comprising the steps of:

(a) withdrawing liquefied cryogenic fuel from a primary storage tank at a low pressure and at a temperature close to the boiling point of the liquefied cryogenic fuel;

(b) feeding the liquefied cryogenic fuel through an indirect heat exchanger;

(c) feeding the liquefied cryogenic fuel to a sparger or mixer chamber;

(d) withdrawing vapor from a vapor space in the primary storage tank and compressing the vapor;

(e) feeding the compressed vapor to a vapor storage tank and storing the vapor therein at a selected pressure;

(f) feeding the vapor from the vapor storage tank through the indirect heat exchanger wherein the vapor is cooled to near a saturation temperature thereof, and alternatively at least partially condensed, the heat from the cooling and condensing of the vapor warming the liquefied cryogenic fuel being fed through the heat exchanger;

(g) sparging the vapor and any condensate exiting the heat exchanger into the liquefied cryogenic fuel in the sparger or mixer chamber, said sparging step condensing the remaining vapor from the heat exchanger;

(h) feeding the warmed liquefied cryogenic fuel from the sparger or mixer chamber into a vehicle fuel tank;

(i) measuring the temperature of the liquefied cryogenic fuel exiting the sparger or mixer chamber; and

(j) providing liquefied cryogenic fuel at a selected equilibrium pressure to the vehicle fuel tank by varying a flow rate of the vapor exiting the vapor storage tank in response to the temperature of the liquefied cryogenic fuel exiting the sparger chamber.

11. The method of claim 10 wherein the step of measuring the temperature of the liquefied cryogenic fuel is performed with a temperature sensor which communicates a signal indicative of equilibrium temperature and pressure to a controller and including the step of determining with the controller, in response to the signal from the temperature sensor, a flow rate of the vapor into the heat exchanger.

12. The method of claim 11 further comprising providing a monitor communicating with the temperature sensor, said monitor comprising an equilibrium pressure readout corresponding to a temperature value detected by the temperature sensor and a manual override of the controller.

13. The method of claim 10 further comprising the step of reducing an internal pressure of a vehicle fuel tank by allowing fuel to flow from the vehicle fuel tank to the primary insulated storage tank.

14. The method of claim 10 further comprising the step of removing liquefied cryogenic fuel from a vehicle fuel tank by flowing vapor directly from the vapor storage tank directly into the vehicle fuel tank.

15. A fuel delivery apparatus comprising:

(a) a primary storage tank for storing liquefied cryogenic fuel, said tank having a vapor space;

(b) a vapor storage tank in communication with the vapor space of the primary storage tank, said vapor storage tank for storing vapor from the primary storage tank at a selected pressure greater than a pressure in the primary storage tank;

(c) means for warming liquefied cryogenic fuel from the primary storage tank by indirect transfer of heat from vapor from the vapor storage tank to the liquefied cryogenic fuel and subsequent transfer of heat of condensation of the vapor to the liquefied cryogenic fuel, said cryogenic fuel warming means in communication with both the primary storage tank and the vapor storage tank;

(d) means for dispensing warmed liquefied cryogenic fuel from the cryogenic fuel warming means, said dispensing means in communication with said warming means and connectable to a vehicle fuel tank;

(e) a temperature sensor disposed in the dispensing means; and

(f) means for controlling a flow rate of vapor from the vapor storage tank to the cryogenic fuel warming means in response to a signal from the temperature sensor, said control means in communication with the vapor storage tank.

16. The apparatus of claim 15 wherein the warming means comprises:

(a) a heat exchanger in communication with both the primary storage tank and the vapor storage tank and disposed directly downstream therefrom with respect to directions of flow of liquefied cryogenic fuel and vapor, respectively, through the heat exchanger, said heat exchanger for warming the liquefied cryogenic fuel and cooling the vapor to near a saturation temperature thereof; and

(b) means for combining the liquefied cryogenic fuel exiting the heat exchanger and the vapor exiting the heat exchanger.

17. The apparatus of claim 16 wherein the means for combining the liquefied cryogenic fuel and the vapor is a sparger or mixer chamber.

18. The apparatus of claim 15 wherein the means for dispensing warmed liquefied cryogenic fluid is an insulated hose having a vehicle tank coupling.

19. The apparatus of claim 15 wherein the means for controlling the flow rate of vapor from the vapor storage tank comprises:

(a) a conduit communicating with the vapor storage tank and the heat exchanger;

(b) a valve disposed in the conduit; and

(c) a controller in communication with the valve and the temperature sensor, said sensor communicating a signal indicative of equilibrium temperature and pressure to the controller.

20. The apparatus of claim 19 further comprising a monitor communicating with the temperature sensor, said monitor comprising an equilibrium pressure readout corresponding to a temperature value detected by the temperature sensor and a manual override of the controller.

21. The apparatus of claim 15 further comprising a conduit communicating with the dispensing means, the conduit receiving fluid from a vehicle fuel tank and feeding fluid to the primary tank to reduce internal pressure of the vehicle fuel tank.

22. The apparatus of claim 15 further comprising a conduit communicating with the vapor storage tank and the fuel dispensing means, the conduit for receiving pressurized vapor from the vapor storage tank and feeding the vapor to the vehicle fuel tank.

23. A fuel delivery apparatus comprising:

(a) a primary storage tank for storing liquefied cryogenic fuel, said tank having a vapor space;

(b) a first conduit having a compressor disposed therein and communicating with the vapor space of the primary storage tank;

(c) a vapor storage tank communicating with the first conduit, said vapor storage tank for storing vapor from the primary storage tank at a selected pressure greater than a pressure in the primary storage tank;

(d) a second conduit in communication with the vapor storage tank having a valve disposed therein;

(e) a third conduit in communication with liquefied cryogenic fuel disposed in the primary storage tank;

(f) a heat exchanger for transferring heat from vapor fed through said second conduit to liquefied cryogenic fuel being fed through said third conduit;

(g) a sparger or mixer chamber in communication with both said second conduit arid said third conduit;

(h) a fourth conduit communicating with a downstream portion of the sparger or mixer chamber with respect to a direction of flow of fluid through the sparger or mixer chamber;

(i) a temperature sensor disposed in the fourth conduit; and

(j) means for controlling a flow rate of vapor through the second conduit in response to a signal from the temperature sensor, said control means in communication with the valve in the second conduit.

24. The apparatus of claim 23 wherein the fourth conduit comprises an insulated hose having a vehicle tank coupling.

25. The apparatus of claim 23 further comprising a monitor communicating with the temperature sensor, said monitor comprising an equilibrium pressure readout corresponding to a temperature value detected by the temperature sensor and a manual override of the controller.

26. The apparatus of claim 23 further comprising a fifth conduit connected to the third conduit for withdrawing liquefied cryogenic fuel from the primary storage tank and returning the cryogenic fuel to the primary storage tank.

27. The apparatus of claim 23 further comprising a fifth conduit communicating with the fourth conduit and having means for communicating with a vehicle fuel tank, the fifth conduit for receiving fluid from a vehicle fuel tank and feeding fluid to the primary tank to reduce internal pressure of the vehicle fuel tank.

28. The apparatus of claim 24 further comprising a fifth conduit in communication with the vapor storage tank and the vehicle tank coupling, the fifth conduit for receiving pressurized vapor from the vapor storage tank and feeding the pressurized vapor to the vehicle fuel tank.