Process for liquefying methane
OwnerCharles L. Newtoninventor
Life of this patent
Estimating the term…
Abstract
A process for liquefying natural gas in which heavier hydrocarbons are separated in a scrub column from the natural gas prior to liquefaction. The feed to the scrub column is intercooled against the methane-rich overhead from said column and isentropically expanded before being introduced to the column and separated from the heavier hydrocarbons. The methane-rich overhead stream is compressed utilizing the mechanical energy of expansion and liquefied in a refrigerated heat exchanger.
Claims7
In a liquefaction process for natural gas wherein heavy hydrocarbons can be separated and recovered in which the natural gas is initially cooled against a first, high level refrigerant before being passed to a scrub column for separation of at least some heavy hydrocarbons and is then subsequently cooled, liquefied and subcooled against a second, low level refrigerant in a main heat exchanger, the improvement comprising providing liquid reflux to the scrub column by expanding the precooled natural gas feed isentropically while obtaining mechanical energy and delivering the expanded feed to the top of said scrub column as a feed and as all of the reflux to said column while removing a methane-rich overhead from said column and recompressing it in a compressor driven by said expander and delivering the recompressed methane-rich overhead stream directly to the main heat exchanger for liquefaction as product.
A liquefaction process for natural gas including the separation in a scrub column of heavier hydrocarbons as a bottom stream from a methane-rich fraction as an overhead stream, comprising the steps of:
- (a) introducing a natural gas feed stream into the liquefaction system at a pressure in the range of 600-2000 psia;
- (b) cooling the feed stream in a series of heat exchangers in indirect heat exchange with a first refrigerant in a closed refrigeration system;
- (c) reducing the pressure of the feed stream to a pressure which is below the critical pressure of both the overhead and bottom streams by isentropically expanding said feed stream while obtaining mechanical energy;
- (d) introducing the expanded feed stream as feed and as all of the reflux to the scrub column to separate the methane-rich fraction as an overhead stream;
- (e) compressing the overhead stream to a high pressure in a compressor utilizing the mechanical energy derived from the expansion of step (c);
- (f) cooling, liquefying and subcooling the methane-rich stream in a heat exchanger by indirect heat exchange with a second, multi-component, refrigerant in a closed refrigeration system;
- (g) withdrawing said liquefied and subcooled methane-rich stream as an LNG product.
A liquefaction process for natural gas including the separation in a scrub column of heavier hydrocarbons as a bottom stream from a methane-rich fraction as an overhead stream, comprising the steps of:
- (a) introducing a natural gas feed stream into the liquefaction system at a pressure in the range of 600-2000 psia;
- (b) cooling the feed stream in a series of heat exchangers in indirect heat exchange with a first refrigerant in a closed refrigeration system;
- (c) reducing the pressure of the feed stream to a pressure which is below the critical pressure of both the overhead and bottom streams by a combination of isentropically expanding said feed stream while obtaining mechanical energy and intercooling at least a portion of the feed stream against the methane-rich overhead stream from the scrub column;
- (d) introducing the intercooled and expanded feed stream as feed and as all of the reflux to the scrub column to separate the methane-rich fraction as an overhead stream and the heavier hydrocarbon fraction as a bottom stream;
- (e) warming the methane-rich overhead stream in an intercooling heat exchange against the intercooling feed stream of step (c);
- (f) compressing the warmed overhead stream to a high pressure in a compressor utilizing the mechanical energy derived from the expansion of step (c);
- (g) cooling, liquefying and subcooling the methane-rich stream in a heat exchanger by indirect heat exchange with a second, multi-component, refrigerant in a closed refrigeration system;
- (h) withdrawing said liquefied and sub-cooled methane-rich stream as an LNG product.
Dependencies are inferred from the claim text.