U.S. patents available from 1976 to present.
U.S. patent applications available from 2005 to present.

Apparatus and method for energy conversion using gas hydrates

Patent 5613362 Issued on March 25, 1997. Estimated Expiration Date: Icon_subject October 6, 2014. Estimated Expiration Date is calculated based on simple USPTO term provisions. It does not account for terminal disclaimers, term adjustments, failure to pay maintenance fees, or other factors which might affect the term of a patent.

Patent References

427400

609430

750493

Ocean thermal gradient power plant
Patent #: 3967449
Issued on: 07/06/1976
Inventor: Beck

Gas recovery from hydrate reservoirs
Patent #: 4007787
Issued on: 02/15/1977
Inventor: Cottle

Multi-use absorption/regeneration power cycle
Patent #: 4009575
Issued on: 03/01/1977
Inventor: Hartman, Jr. ,   et al.

4090361

Mass transport heat exchanger method and apparatus for use in ocean thermal energy exchange power plants
Patent #: 4104883
Issued on: 08/08/1978
Inventor: Naef

Ocean thermal energy conversion system and method for operation
Patent #: 4189924
Issued on: 02/26/1980
Inventor: LaCoste

Power cycles based upon cyclical hydriding and dehydriding of a material
Patent #: 4198827
Issued on: 04/22/1980
Inventor: Terry ,   et al.

More ...

Inventor

Application

No. 319138 filed on 10/06/1994

US Classes:

60/649, Including mixing or separating materials of different chemical compositions in a motive fluid flow path60/641.7, Ocean thermal energy conversion (OTEC)60/651, Including vaporizing a motive fluid other than water60/671, Motive fluid comprises a material other than steam or water60/673One fluid absorbs or reacts with another

Examiners

Primary: Heyman, Leonard E.

Attorney, Agent or Firm

International Class

F01K 025/00

Abstract

An encagement vessel contains water and a working gas capable of forming hydrate with the water. A heat exchange arrangement is associated with the encagement vessel for removing heat from the working gas and water in the encagement vessel to form gas hydrate at an initial temperature. A working gas supply continues to add working gas to the encagement vessel as heat is removed in order to maintain the equilibrium pressure of the gas hydrate at the equilibrium pressure associated with the initial temperature as the hydrate is formed. An equilibrium pressure shifting arrangement increases the equilibrium pressure of the gas hydrate to an end pressure. A dissociating heat exchanger is included for adding heat to the hydrate at the end equilibrium pressure to dissociate the gas hydrate into water and working gas at the end pressure. A suitable gas valve is associated with the vessel in which dissociation is performed in order to remove gas hydrate at the end pressure and maintain the pressure in the vessel at the end pressure as the hydrate is dissociated. The working gas released at the high end pressure may be directed to a suitable gas turbine for driving the turbine to produce mechanical energy that can in turn be used to produce electricity through a suitable generator.

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