LNG regasification and power generation

• US 8,661,820 B2
• Filed: 05/30/2008
• Issued: 03/04/2014
• Est. Priority Date: 05/30/2007
• Status: Expired due to Fees

• Current Assignee: Fluor Technologies Corporation (Fluor Corporation)
• Original Assignee: Fluor Technologies Corporation (Fluor Corporation)
• Inventors: Mak, John
• Primary Examiner(s): NGUYEN, HOANG M
• Application Number:
  US12/598,810
• Publication Number:
  US 20100146971A1
• Time in Patent Office: 2,104 Days
• Field of Search: 606/51, 606/53, 606/71, 60677-679
• US Class Current: 60/651
• CPC Class Codes: F01K 13/00 General layout or general methods of operation of complete plants
• 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 2225/0123 gaseous, e.g. CNG, GNC
• CPC Class Codes: F17C 2225/036 Very high pressure, i.e. above 80 bars
• CPC Class Codes: F17C 2227/0309 using another fluid
• CPC Class Codes: F17C 2227/0313 by forced circulation, e.g. using a fan
• CPC Class Codes: F17C 2227/0316 Water heating
• CPC Class Codes: F17C 2227/0318 using seawater
• CPC Class Codes: F17C 2227/0323 in a closed loop
• CPC Class Codes: F17C 2227/0332 by burning a combustible
• CPC Class Codes: F17C 2227/0397 characterised by fins
• CPC Class Codes: F17C 2265/05 Regasification
• CPC Class Codes: F17C 7/04 with change of state, e.g. vaporisation
• CPC Class Codes: Y02E 10/30 Energy from the sea, e.g. using wave energy or salinity gradient
• CPC Class Codes: Y02E 20/16 Combined cycle power plant [CCPP], or combined cycle gas turbine [CCGT]

Abstract

LNG is regasified with concurrent power production in systems and methods where the refrigeration content of the LNG condenses a low pressure working fluid vapor and in which the combined refrigeration content of the warmed LNG and low pressure working fluid condensate condenses an intermediate pressure working fluid vapor.

Claims

1. A method of regasification of LNG and producing power, the method comprising:

expanding a working fluid in a first expansion turbine to produce an intermediate pressure working fluid vapor and power;

expanding a first portion of the intermediate pressure working fluid vapor in a second expansion turbine to produce a low pressure working fluid vapor and additional power;

condensing the low pressure working fluid vapor using refrigeration content of to produce a heated LNG and a second condensate;

using refrigeration content of the second condensate and using refrigeration content of the heated LNG to condense a remainder of the intermediate pressure working fluid vapor and to produce a first condensate and vaporized LNG; and

combining the first and second condensates to form the working fluid.

2. The method of claim 1 wherein the step of combining the first and second condensates is performed in a heat exchanger.

3. The method of claim 1 wherein the first and second condensates are formed in respective exchangers in a cold box.

4. The method of claim 1 further comprising heating at least one of the combined condensates and the first portion of the intermediate pressure working fluid vapor.

5. The method of claim 4 wherein the step of heating uses ambient air, seawater, or waste heat as a heat source.

6. The method of claim 1 wherein the combined condensates have a pressure of between 100 and 500 psia before entering the first expansion turbine, wherein the intermediate pressure working fluid vapor has a pressure of between 50 and 250 psia, and wherein the low pressure working fluid vapor has a pressure of between 5 and 50 psia.

7. The method of claim 1 wherein a ratio between the first portion of the intermediate pressure working fluid vapor and the second portion of the intermediate pressure working fluid vapor is at least 1.1.

8. The method of claim 1 wherein the working fluid comprises a hydrocarbon.

9. The method of claim 1 wherein the LNG is regasified at a rate of 500 mM scfd.

10. An LNG regasification and power generation system, the system comprising:

a cold box that is configured to allow condensation of a low stage working fluid vapor using LNG to thereby produce heated LNG and to allow condensation of intermediate stage working fluid vapor using the heated LNG and low stage working fluid condensate, and wherein the cold box is further configured to allow vaporization of the LNG using heat content of the intermediate stage working fluid vapor and heat content of the low stage working fluid vapor;

a first expansion turbine fluidly coupled to the cold box and a second expansion turbine such that the first expansion turbine provides a second portion of the intermediate stage working fluid vapor to the cold box and a first portion of the intermediate stage working fluid vapor to the second expansion turbine;

wherein the second expansion turbine is configured to produce the low stage working fluid vapor; and

wherein the first expansion turbine is configured to receive an intermediate stage working fluid condensate and the low stage working fluid condensate.

11. The system of claim 10 wherein the cold box is configured to allow injection of the low stage working fluid condensate into the intermediate stage working fluid vapor.

12. The system of claim 10 further comprising a heater that is configured to allow heating of the intermediate stage working fluid condensate, the low stage working fluid condensate, or a first portion of the intermediate stage working fluid vapor.

13. The system of claim 12 wherein the heater is configured to use heat content of ambient air, seawater, or waste heat to heat the intermediate stage working fluid condensate, the tow stage working fluid condensate, or a first portion of the intermediate stage working fluid vapor.

14. The system of claim 10 wherein the first expansion turbine is configured to provide the first portion of the intermediate stage working fluid vapor to the cold box at a pressure of between 50 and 250 psia, and wherein the second expansion turbine is configured to produce the low stage working fluid vapor at a pressure of between 5 and 50 psia.

15. The system of claim 10 wherein a ratio of the first portion of the intermediate stage working fluid vapor to the second portion of the intermediate stage working fluid vapor is at least 1.1.