Natural gas liquefaction
A process for liquefying natural gas in conjunction with producing a liquid stream containing predominantly hydrocarbons heavier than methane is disclosed. In the process, the natural gas stream to be liquefied is partially cooled, expanded to an intermediate pressure, and supplied to a distillation column. The bottom product from this distillation column preferentially contains the majority of any hydrocarbons heavier than methane that would otherwise reduce the purity of the liquefied natural gas. The residual gas stream from the distillation column is compressed to a higher intermediate pressure, cooled under pressure to condense it, and then expanded to low pressure to form the liquefied natural gas stream.
1. In a process for liquefying a natural gas stream containing methane and heavier hydrocarbon components wherein
(a) said natural gas stream is cooled under pressure to condense at least a portion of it and form a condensed stream; and
(b) said condensed stream is expanded to lower pressure to form said liquefied natural gas stream;
the improvement wherein
(1) said natural gas stream is treated in one or more cooling steps by a closed loop refrigeration cycle;
(2) said cooled natural gas stream is divided into at least a first gaseous stream and a second gaseous stream;
(3) said first gaseous stream is cooled by a closed loop refrigeration cycle to condense substantially all of it and thereafter expanded to an intermediate pressure;
(4) said second gaseous stream is expanded to said intermediate pressure;
(5) said expanded substantially condensed gaseous first stream and said expanded gaseous second stream are directed into a distillation column wherein said streams are separated into a volatile residue gas fraction containing a major portion of said methane and lighter components and a relatively less volatile fraction containing a major portion of said heavier hydrocarbon components; and
(6) said volatile residue gas fraction is cooled under pressure to condense at least a portion of it and form thereby said condensed stream.
2. In a process for liquefying a natural gas stream containing methane and heavier hydrocarbon components wherein
(a) said natural gas stream is cooled under pressure to condense at least a portion of it and form a condensed stream; and
(b) said condensed stream is expanded to lower pressure to form said liquefied natural gas stream;
the improvement wherein
(1) said natural gas stream is treated in one or more cooling steps by a closed loop refrigeration cycle to partially condense it;
(2) said partially condensed natural gas stream is separated to provide thereby a vapor stream and a liquid stream;
(3) said vapor stream is divided into at least a first gaseous stream and a second gaseous stream;
(4) said first gaseous stream is cooled by a closed loop refrigeration cycle to condense substantially all of it and thereafter expanded to an intermediate pressure;
(5) said second gaseous stream is expanded to said intermediate pressure;
(6) said liquid stream is expanded to said intermediate pressure;
(7) said expanded substantially condensed gaseous first stream, said expanded gaseous second stream, and said expanded liquid stream are directed into a distillation column wherein said streams are separated into a volatile residue gas fraction containing a major portion of said methane and lighter components and a relatively less volatile fraction containing a major portion of said heavier hydrocarbon components; and
(8) said volatile residue gas fraction is cooled under pressure to condense at least a portion of it and form thereby said condensed stream.
3. In a process for liquefying a natural gas stream containing methane and heavier hydrocarbon components wherein
(a) said natural gas stream is cooled under pressure to condense at least a portion of it and form a condensed stream; and
(b) said condensed stream is expanded to lower pressure to form said liquefied natural gas stream;
the improvement wherein
(1) said natural gas stream is treated in one or more cooling steps by a closed loop refrigeration cycle to partially condense it;
(2) said partially condensed natural gas stream is separated to provide thereby a vapor stream and a liquid stream;
(3) said vapor stream is divided into at least a first gaseous stream and a second gaseous stream;
(4) said first gaseous stream is combined with at least a portion of said liquid stream, forming thereby a combined stream;
(5) said combined stream is cooled by a closed loop refrigeration cycle to condense substantially all of it and thereafter expanded to an intermediate pressure;
(6) said second gaseous stream is expanded to said intermediate pressure;
(7) any remaining portion of said liquid stream is expanded to said intermediate pressure;
(8) said expanded substantially condensed combined stream, said expanded gaseous second stream, and said remaining portion of said liquid stream are directed into a distillation column wherein said streams are separated into a volatile residue gas fraction containing a major portion of said methane and lighter components and a relatively less volatile fraction containing a major portion of said heavier hydrocarbon components; and
(9) said volatile residue gas fraction is cooled under pressure to condense at least a portion of it and form thereby said condensed stream.
4. The improvement according to claim 1 , 2 , or 3 wherein said volatile residue gas fraction is compressed and thereafter cooled under pressure to condense at least a portion of it and form thereby said condensed stream.
5. The improvement according to claim 1 , 2 , or 3 wherein said volatile residue gas fraction is heated by means other than with heat exchange with said natural gas stream, compressed, and thereafter cooled under pressure to condense at least a portion of it and form thereby said condensed stream.
6. The improvement according to claim 1 , 2 , or 3 wherein said volatile residue gas fraction contains a major portion of said methane, lighter components, and C 2 components.
7. The improvement according to claim 1 , 2 , or 3 wherein said volatile residue gas fraction contains a major portion of said methane, lighter components, C 2 components, and C 3 components.