Process and plant for producing liquefied natural gas

Patent metadata

Field	Value
Publication number	US-11603496-B2
Application number	US-201816772193-A
Country	US
Kind code	B2
Filing date	Dec 3, 2018
Priority date	Dec 12, 2017
Publication date	Mar 14, 2023
Grant date	Mar 14, 2023

Abstract

The invention relates to a process (100) for producing liquefied natural gas using a feedstock mixture that contains at least methane, one or more components boiling at a temperature lower than methane and one or more hydrocarbons boiling at a temperature higher than methane, wherein the hydrocarbon(s) boiling at a temperature higher than methane comprise one or more hydrocarbons freezing at a higher temperature, with a freezing point higher than −50° C. According to the invention the feedstock mixture is fed into a pressure swing adsorption process (10), in which a first fraction containing methane and a second fraction containing methane are formed, the first fraction containing methane contains, in addition to the methane, at least the predominant portion of the components of the feedstock mixture that boil more readily than methane and is low in or free from the hydrocarbons boiling less readily than methane, and the second fraction containing methane contains, in addition to the methane, at least the predominant portion of the hydrocarbons from the feedstock that boil less readily than methane and is low in or free from the components that boil more readily than methane, and the first fraction containing methane, or a portion thereof, is supplied for liquefaction (20). The invention also relates to a corresponding plant.

First claim

The invention claimed is:

1. A process ( 100 ) for producing liquefied natural gas using a feedstock mixture that contains at least methane, one or more components boiling at a temperature lower than methane, and one or more hydrocarbons boiling at a temperature higher than methane, wherein the hydrocarbon(s) boiling at a temperature higher than methane have one or more high-freezing hydrocarbons with a freezing point higher than −50° C.,
said process comprising:
feeding the feedstock mixture to a pressure swing adsorption process ( 10 ), in which a first fraction containing methane and a second fraction containing methane are formed,
wherein the first fraction containing methane contains, in addition to the methane, at least the predominant portion of the components of the feedstock mixture that boil more readily than methane and is low in or free from the hydrocarbons boiling less readily than methane,
wherein the second fraction containing methane contains, in addition to the methane, at least the predominant portion of the hydrocarbons of the feedstock that boil less readily than methane and is low in or free from the components boiling more readily than methane,
subjecting the first fraction containing methane, or a portion thereof, is to liquefaction ( 20 ),
obtaining the second fraction containing methane from the pressure swing adsorption process at an absolute pressure level of 0.1 to 5 bar, and subjecting the second fraction containing methane, or a portion thereof, to compression ( 30 ), and
wherein, after the compression ( 30 ), the second fraction containing methane, or the portion thereof supplied for compression ( 30 ), is at least partially supplied to thermal separation ( 40 ), and the thermal separation ( 40 ) is carried out using a rectification column which is operated in such a way that hydrocarbons having less than two carbon atoms transition at least predominantly into an overhead gas, hydrocarbons having two carbon atoms transition at least predominantly into the overhead gas, and hydrocarbons having three or more carbon atoms transition at least predominantly into a bottoms liquid.

2. The process ( 100 ) according to claim 1 , wherein the first fraction containing methane is provided by means of the pressure swing adsorption process ( 10 ) at an absolute pressure level of 20 to 40 bar, and wherein the first fraction containing methane, or the portion thereof supplied to the liquefaction ( 20 ), is supplied to the liquefaction ( 20 ) at this absolute pressure level.

3. The process ( 100 ) according to claim 1 , wherein the hydrocarbons boiling less readily than methane in the feedstock mixture and in the second fraction containing methane comprise propane and/or at least one butane, and are selected in the compression ( 30 ) as a function of the content of propane and/or of the at least one butane in the second fraction containing methane, or the portion thereof supplied for thermal separation ( 40 ).

4. The process ( 100 ) according to claim 1 , wherein said overhead gas is low in or free from the high-freezing hydrocarbons.

5. The process ( 100 ) according to claim 4 , wherein a portion of the overhead has is also subjected to liquefaction ( 20 ).

6. The process according to claim 1 , wherein the overhead temperature of the rectification column is below the solidification temperature of the high-freezing hydrocarbons.

7. A process ( 100 ) for producing liquefied natural gas using a feedstock mixture that contains at least methane, one or more components boiling at a temperature lower than methane, and one or more hydrocarbons boiling at a temperature higher than methane, wherein the hydrocarbon(s) boiling at a temperature higher than methane have one or more high-freezing hydrocarbons with a freezing point higher than −50° C., said process comprising:
feeding the feedstock mixture to a pressure swing adsorption process ( 10 ), in which a first fraction containing methane and a second fraction containing methane are formed,
wherein the first fraction containing methane contains, in addition to the methane, at least the predominant portion of the components of the feedstock mixture that boil more readily than methane and is low in or free from the hydrocarbons boiling less readily than methane,
wherein the second fraction containing methane contains, in addition to the methane, at least the predominant portion of the hydrocarbons of the feedstock that boil less readily than methane and is low in or free from the components boiling more readily than methane,
subjecting the first fraction containing methane, or a portion thereof, is to liquefaction ( 20 ),
obtaining the second fraction containing methane from the pressure swing adsorption process at an absolute pressure level of 0.1 to 5 bar, and subjecting the second fraction containing methane, or a portion thereof, to compression ( 30 ), and

wherein, after the compression ( 30 ), the seocnd fraction containing methane, or the portion thereof supplied for compression ( 30 ), is at least partially supplied to thermal separation ( 40 ), and the thermal separation ( 40 ) is carried out using a rectification column which is operated in such a way that hydrocarbons having less than less carbon atoms transition at least predominantly into the overhead gas, hydrocarbons having three carbon atoms transition at least predominantly into an overhead gas, hydrocarbons having less than three carbon atoms transition at least predominantly into the overhead has, and hydrocarbons having four or more carbon atoms transition at least predominantly into a bottoms liquid.

8. The process ( 100 ) according to claim 1 , wherein the feedstock mixture is obtained by conditioning ( 50 ) natural gas, wherein the conditioning ( 50 ) comprises drying and carbon dioxide removal.

9. The process ( 100 ) according to claim 1 , wherein the feedstock mixture is provided at a first pressure level and fed to the pressure swing adsorption process ( 10 ) at a second pressure level, wherein the feedstock mixture is at least partially brought to the second pressure level by expansion ( 60 ) in one or more expansion machines.

10. The process ( 100 ) according to claim 9 , wherein one or more compressors used to compress ( 30 ) the second fraction containing methane, or the portion thereof supplied for compression ( 30 ), are driven by means of the one or more expansion machines.

11. The process ( 100 ) according to claim 8 , wherein said conditioning ( 50 ) comprises a temperature swing adsorption process.

12. The process according to claim 7 , wherein the overhead temperature of the rectification column is below the solidification temperature of the high-freezing hydrocarbons.

13. A plant for producing liquefied natural gas using a feedstock mixture containing at least methane, one or more components boiling at a temperature lower than methane, and one or more hydrocarbons boiling at a temperature higher than methane, wherein the hydrocarbon or hydrocarbons boiling at a temperature higher than methane have one or more high-freezing hydrocarbons with a freezing point of more than −50° C., said plant comprising:
means adapted to supply the feedstock mixture to a pressure swing adsorption process ( 10 ) and to form there a first fraction containing methane and a second fraction containing methane,
wherein the first fraction containing methane contains, in addition to the methane, at least the predominant portion of the components of the feedstock mixture that boil more readily than methane and is low in or free from the hydrocarbons boiling less readily than methane,
wherein the second fraction containing methane c

Assignees

• Linde Gmbh

Inventors

• Fritz Helmut
• Leitmayr Werner
• Keller Tobias
• Voss Christian

Classifications

• F25J2240/02

  Expansion of a process fluid in a work-extracting turbine (i.e. isentropic expansion), e.g. of the feed stream · CPC title

• C10L3/101

  Removal of contaminants · CPC title

• F25J3/0233

  separation of CnHm with 1 carbon atom or more · CPC title

• F25J2205/40

  using hybrid system, i.e. combining cryogenic and non-cryogenic separation techniques · CPC title

• F25J2260/20

  Integration in an installation for liquefying or solidifying a fluid stream · CPC title