| US 7,600,396 B2 | ||
| Power cycle with liquefied natural gas regasification | ||
| John Mak, Santa Ana, Calif. (US) | ||
| Assigned to Fluor Technologies Corporation, Aliso Viejo, Calif. (US) | ||
| Appl. No. 10/559,171 PCT Filed Aug. 26, 2003, PCT No. PCT/US03/26805 § 371(c)(1), (2), (4) Date Jun. 27, 2006, PCT Pub. No. WO2004/109180, PCT Pub. Date Dec. 16, 2004. |
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| Claims priority of provisional application 60/476770, filed on Jun. 05, 2003. | ||
| Prior Publication US 2007/0101732 A1, May 10, 2007 | ||
| Int. Cl. F25J 3/00 (2006.01); F17C 9/02 (2006.01) | ||
| U.S. Cl. 62—620 [62/50.2] | 22 Claims |

| 1. A regasification plant for liquefied natural gas comprising:
a liquefied natural gas fractionation unit that forms a process product from the liquefied natural gas;
a cooler and a pump fluidly coupled to the fractionation unit and configured to allow liquefaction and pressurization of the
process product to so form a liquefied and pressurized process product;
a heat source fluidly coupled to the pump and configured to heat the liquefied and pressurized process product to thereby
produce a heated process product; and
wherein at least one component of the fractionation unit uses refrigeration content of the liquefied natural gas, and wherein
an expander expands the heated process product to produce work.
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