Fluid bypass method and system for controlling the temperature of a non-petroleum fuel

Patent metadata

Field	Value
Publication number	US-10961109-B2
Application number	US-201916532682-A
Country	US
Kind code	B2
Filing date	Aug 6, 2019
Priority date	Nov 16, 2018
Publication date	Mar 30, 2021
Grant date	Mar 30, 2021

Abstract

A fluid bypass method for controlling the temperature of a non-petroleum fuel, the fluid bypass method includes: providing a fuel at a pressure sufficient to effect a desired flow rate to a vehicle, the fuel being at a liquid or substantially supercritical thermodynamic state requiring further heat addition in a vaporizer; and diverting a bypass stream with partial or no vaporization to a heat exchanger as a cold fluid on a cold side of the heat exchanger. The method further includes providing a remainder stream of the fuel to the vaporizer; mixing the remainder stream outflowed from the vaporizer with the cold fluid outflowed from the cold side of the heat exchanger to form a combined fuel stream; and providing the combined fuel stream to the heat exchanger as a warm fluid on a warm side of the heat exchanger.

First claim

The invention claimed is:

1. A fluid bypass method for controlling temperature of a non-petroleum fuel, the method comprising the steps:
providing the non-petroleum fuel, said non-petroleum fuel being in a liquid or substantially supercritical thermodynamic state;
diverting a bypass stream of at least a first portion of the non-petroleum fuel having partial or no vaporization to a heat exchanger via a bypass line;
providing the bypass stream to a cold side of the heat exchanger;
providing a second portion of the non-petroleum fuel to a vaporizer, for heating the second portion in the vaporizer to provide a heated second portion;
mixing the heated second portion of the non-petroleum fuel from the vaporizer with the bypass stream from the heat exchanger to form a combined fuel stream;
providing the combined fuel stream to the heat exchanger on a warm side of the heat exchanger, to obtain a cooled combined fuel stream.

2. The fluid bypass method according to claim 1 , wherein the non-petroleum fuel is liquefied natural gas, and the method further comprises a step of supplying the cooled combined fuel stream to at least one vehicle.

3. The fluid bypass method according to claim 1 , wherein the non-petroleum fuel is liquid hydrogen, and the method further comprises a step of supplying the cooled combined fuel stream to the at least one vehicle.

4. The fluid bypass method according to claim 3 , wherein a fraction of the bypass stream ranges from 5% to 95%.

5. The fluid bypass method according to claim 3 , wherein a temperature of the combined fuel stream ranges from −15° C. to 20° C.

6. The fluid bypass method according to claim 3 , wherein the heat exchanger is a recuperative heat exchanger.

7. The fluid bypass method according to claim 6 , wherein the heat exchanger is an aluminum core heat exchanger, and the first portion is taken at a point midway in the vaporizer.

8. The fluid bypass method according to claim 1 , wherein the pressure is a desired vehicle pressure ranging from 20 MPa to 100 MPa.

9. The fluid bypass method according to claim 1 , wherein a dispensing temperature for dispensing the non-petroleum fuel into the at least one vehicle ranges from −50° C. to 30° C.

10. The fluid bypass method according to claim 1 , wherein an amount of the second portion in the bypass stream is controlled with at least one controllable valve to maintain a dispensing temperature at a dispensing temperature setpoint for supplying the fuel to the at least one vehicle.

11. The method according to claim 10 , wherein before the supplying of the fuel stream to the vehicle is completed, the bypass stream is equalized to a temperature equal to the dispensing temperature.

12. The method according to claim 1 , further comprising the step of diverting at least a third portion of the fuel from the vaporizer to the bypass line, wherein said third portion is at least partially vaporized in the vaporizer.

13. The method according to claim 1 , further comprising a step of supplying the cooled combined fuel stream to the at least one vehicle, and a step of providing the non-petroleum fuel to at least a second vehicle, wherein the diverted bypass stream is split into a first bypass stream and a second bypass stream, wherein said first bypass stream is diverted to the heat exchanger for cooling the combined fuel stream to the at least one vehicle and said second bypass stream is diverted to a second heat exchanger for cooling a second combined fuel stream to the second vehicle.

14. The method according to claim 1 , further comprising a dispenser for supplying the cooled combined fuel stream to the at least one vehicle, said dispenser comprising a flow meter, a pressure regulator, a nozzle, and the heat exchanger.

15. A non-transitory computer readable storage medium that stores a computer program comprising the fluid bypass method for controlling the temperature of a non-petroleum fuel according to claim 1 , which when executed by a processor, is implemented on a computer.

Assignees

• China Energy Investment Corp Ltd
• Nat Inst Clean & Low Carbon Energy

Inventors

• Li Xianming Jimmy
• Youn Edward
• Pickles Jeff
• Singh Surinder

Classifications

• Y02E60/32

  Hydrogen storage · CPC title

• F17C2270/0139

  Fuel stations · CPC title

• F17C2265/065

  for refuelling vehicle fuel tanks · CPC title

• F17C2265/022

  identical fluid · CPC title

• F17C2250/0443

  Flow or movement of content · CPC title