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US4036028A Expired / Lapsed US ⏱️ 0.0 years remaining

Process and apparatus for evaporating and heating liquified natural gas

Assignee: Sulzer AG
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Filing: 1975-10-30
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Granted: 1977-07-19
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Expires: 1995-10-30
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Abstract

Abstract The waste heat of an open gas turbine system used to heat a flow of liquified natural gas is recovered and passed via an intermediate heat exchange circuit or system to the flow of liquified natural gas. The intermediate circuit uses hydrocarbons which may or may not have been halogen-substituted as the heat exchange medium. The heat is extracted from the flue by closed piping systems which use water as a heat carrier as well as a system which uses an anti-freeze agent such as methanol. The anti-freeze circuit permits injection of the anti-freeze agent into the intake of the gas turbine while a rectifying column allows recovery of the anti-freeze agent. The intermediate circuit includes a vapor turbine which expands the hydrocarbon medium after the hydrocarbon medium receives heat in order to produce useful work.

Inventors

  • 👤 Charles Mandrin

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-29 04:40
CPC Classifications
F; F01; F01K; F01K23/00; F01K23/02; F02; F02C; F02C6/00; F02C6/18; F02C7/00; F02C7/12; F02C7/14; F02C7/141; F02C7/143; F17; F17C; F17C9/00; F17C9/02; F17C2265/00; F17C2265/05; Y; Y02; Y02T; Y02T10/00; Y02T10/10; Y02T10/12

Claims Analysis

Total Claims: 9
Claim 1
Independent Claim 251 words
An apparatus for evaporating and heating liquid natural gas comprising means defining a predetermined flow path for a flow of liquid natural gas; an open gas turbine system having an air intake and an exhaust flue for a flow of hot exhaust gases; a first heat exchange system for cooling air taken into said air intake and for heating the flow of liquid natural gas; a second heat exchange system for extracting heat from the flow of exhaust gases in said flue and for heating the flow of natural gas with the extracted heat, said second heat exchange system including a first closed piping system having a hydrocarbon heat exchange medium therein, a first heat exchanger for receiving heat from the flow of exhaust gases to heat the hydrocarbon medium, a second heat exchanger for heating of the natural gas in said flow path in heat exchange relation with the hydrocarbon medium, a compressor means downstream of said second heat exchanger in said flow path for compressing the hydrocarbon medium and a vapor turbine upstream of said second heat exchanger in said flow path for expanding the hydrocarbon medium to produce work; means for admixing an anti-freeze agent into said gas turbine system air intake; and a rectifying means for receiving and vaporizing the anti-freeze agent downstream of said air intake, said rectifying means having a head product removal line connected to a third heat exchanger in said first closed piping system for receiving heat from the flow of exhaust gas.
Claim 2
Independent Claim 251 words
An apparatus for evaporating and heating liquid natural gas comprising means defining a predetermined flow path for a flow of liquid natural gas; an open gas turbine system having an air intake and an exhaust flue for a flow of hot exhaust gases; a first heat exchange system for cooling air taken into said air intake and for heating the flow of liquid natural gas; a second heat exchange system for extracting heat from the flow of exhaust gases in said flue and for heating the flow of natural gas with the extracted heat, said second heat exchange system including a first closed piping system having a hydrocarbon heat exchange medium therein, a first heat exchanger for receiving heat from the flow of exhaust gases to heat the hydrocarbon medium, a second heat exchanger for heating of the natural gas in said flow path in heat exchange relation with the hydrocarbon medium, a compressor means downstream of said second heat exchanger in said flow path for compressing the hydrocarbon medium and a vapor turbine upstream of said second heat exchanger in said flow path for expanding the hydrocarbon medium to produce work; means for admixing an anti-freeze agent into said gas turbine system air intake; and a rectifying means for receiving and vaporizing the anti-freeze agent downstream of said air intake, said rectifying means having a head product removal line connected to a third heat exchanger in said first closed piping system for receiving heat from the flow of exhaust gas.
Claim 3
Dependent Claim 77 words
An apparatus as set forth in claim 1 which further comprises a second closed piping system for a heat carrier, said second closed piping system passing in heat exchange relation with said first heat exchanger in said first closed piping system and including a fourth heat exchanger in said flue to transfer heat from the exhaust gases to said heat carrier and a pump for pumping the heat carrier to said fourth heat exchanger in said flue.
Claim 4
Dependent Claim 24 words
An apparatus as set forth in claim 1 which further includes a burner in said exhaust flue for supplemental heating of the exhaust gases.
Claim 5
Dependent Claim 172 words
A process for evaporating and heating liquid natural gas comprising the steps of passing a flow of liquid natural gas through a predetermined flow path; generating a flow of hot exhaust gases in a flue of an open gas turbine system; passing a flow of hydrocarbon heat exchange medium through a closed piping system for evaporation under heat extracted from the flow of exhaust gases, subsequent expansion with the performance of work, liquifaction under a heat exchange relation with the flow of liquid natural gas in said flow path wherein heat is delivered to the liquid natural gas, and compression at an elevated pressure; admixing a water-miscible anti-freeze agent into an air flow delivered to the gas turbine system; rectifying a condensed mixed phase of said agent and moisture from the air flow under a portion of the waste heat of said flow of exhaust gases to obtain a gaseous head product; and passing the gaseous head product into heat exchange relation with said compressed hydrocarbon medium to condense the head product.
Claim 6
Dependent Claim 172 words
A process for evaporating and heating liquid natural gas comprising the steps of passing a flow of liquid natural gas through a predetermined flow path; generating a flow of hot exhaust gases in a flue of an open gas turbine system; passing a flow of hydrocarbon heat exchange medium through a closed piping system for evaporation under heat extracted from the flow of exhaust gases, subsequent expansion with the performance of work, liquifaction under a heat exchange relation with the flow of liquid natural gas in said flow path wherein heat is delivered to the liquid natural gas, and compression at an elevated pressure; admixing a water-miscible anti-freeze agent into an air flow delivered to the gas turbine system; rectifying a condensed mixed phase of said agent and moisture from the air flow under a portion of the waste heat of said flow of exhaust gases to obtain a gaseous head product; and passing the gaseous head product into heat exchange relation with said compressed hydrocarbon medium to condense the head product.
Claim 7
Dependent Claim 31 words
A process as set forth in claim 4 which further comprises the step of extracting heat from the expanded hydrocarbon medium prior to liquification for delivery to the compressed hydrocarbon medium.
Claim 8
Dependent Claim 52 words
A process as set forth in claim 4 which further comprises the step of passing a heat carrier through the flue of the open gas turbine system in heat exchange relation to extract heat therefrom for delivery to the hydrocarbon heat exchange medium in the closed piping system for said evaporation thereof.
Claim 9
Dependent Claim 18 words
A process as set forth in claim 4 which further comprises the step of reheating the exhaust gases.

References Cited (Backward Citations)

US2593963A Cited
US3068659A Cited
US3183666A Cited
US3331214A Cited
US3535210A Cited
US3438216A Cited
US3867811A Cited
US3770048A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1980-07-18 1981-01-17 1981-07-19 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1984-07-18 1985-01-17 1985-07-19 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1988-07-18 1989-01-17 1989-07-19 $7700.00 Window Closed / Lapsed

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