Method for producing a flow rich in methane and a flow rich in c2+ hydrocarbons, and associated installation

Patent metadata

Field	Value
Publication number	US-2016370109-A9
Application number	US-201514747417-A
Country	US
Kind code	A9
Filing date	Jun 23, 2015
Priority date	Jul 9, 2009
Publication date	Dec 22, 2016
Grant date	—

Abstract

This method envisions cooling the supply flow in a first heat exchanger, separation in a first separation flask in order to produce a light upper flow and a heavy lower flow and dividing the light upper flow into a supply fraction of a dynamic pressure reduction turbine and a supply fraction of a first distillation column. A cooled reflux flow is formed from an effluent from a dynamic pressure reduction turbine, the portion of the effluent being cooled and at least partially liquefied in a heat exchanger. The cooled reflux flow is introduced from the heat exchanger into the first distillation column.

First claim

What is claimed is:

1 . A method of producing a flow rich in methane and a flow rich in C2+ hydrocarbons from a supply flow containing hydrocarbons, the method comprising:
separating the supply flow into a first fraction of the supply flow and at least a second fraction of the supply flow; introducing the first fraction of the supply flow into a first heat exchanger; cooling the first fraction of the supply flow in the first heat exchanger; introducing the cooled first fraction of the supply flow into a first separation flask in order to produce a light upper flow and a heavy lower flow; dividing the light upper flow into a turbine supply fraction and a column supply fraction; pressure reducing the turbine supply fraction in a first dynamic pressure reduction turbine and introducing at least a portion of the turbine supply fraction subjected to pressure reduction into the first turbine in a middle portion of a first distillation column; cooling and at least partially condensing the column supply fraction and pressure reducing and introducing at least a portion of the cooled column supply fraction into an upper portion of the first distillation column; introducing the heavy lower flow into a second separation flask in order to produce an upper gas fraction and a lower liquid fraction; pressure reducing the lower liquid fraction and introducing the lower liquid fraction in the middle portion of the first distillation column; cooling and at least partially condensing the upper gas fraction; recovering a lower column flow at the bottom of the first distillation column, the flow rich in C 2 + hydrocarbons being formed from the lower column flow; recovering and reheating of an upper column flow rich in methane; compressing at least a fraction of the upper column flow in at least a first compressor coupled to the first dynamic pressure reduction turbine and in at least a second compressor; forming the flow rich in methane from the reheated and compressed upper column flow; removing an extraction flow from the upper column flow; cooling the extraction flow in a second heat exchanger and introducing the cooled extraction flow into an upper portion of the first distillation column; introducing at least a portion of the second fraction of the supply flow into a second dynamic pressure reduction turbine, separate from the first dynamic pressure reduction turbine; forming an effluent from the second dynamic pressure reduction turbine; cooling and at least partly liquefying at least a portion of the effluent from the second dynamic pressure reduction turbine in a downstream heat exchanger in heat exchange relationship with at least a fraction of the upper column flow, the downstream heat exchanger being separate from the second heat exchanger; forming a cooled reflux flow from the portion of the effluent cooled in the downstream heat exchanger; and introducing the cooled reflux flow from the downstream heat exchanger into the first distillation column.

2 . The method according to claim 1 , wherein an upper gas flow obtained from the portion of the effluent cooled in the downstream heat exchanger is introduced into an auxiliary distillation column, the cooled reflux flow being formed from a lower flow of the auxiliary distillation column.

3 . The method according to claim 2 , further comprising:
introducing the effluent from the second dynamic pressure reduction turbine into a downstream separation flask in order to form at the top of the downstream separation flask the upper gas flow and at the bottom of the downstream separation flask a third lower liquid flow; and cooling the upper gas flow in the downstream heat exchanger and introducing the cooled upper gas flow in the auxiliary column.

4 . Method according to claim 2 , comprising producing an upper auxiliary flow from the auxiliary distillation column and mixing the upper auxiliary flow with the upper column flow rich in methane produced by the first distillation column.

5 . Method according to claim 2 , wherein at least a portion of the cooled and at least partially condensed upper gas fraction is introduced in the auxiliary distillation column.

6 . Method according to claim 2 , wherein a first portion of the cooled column supply fraction is introduced in the auxiliary distillation column, a second portion of the cooled column supply fraction being introduced directly into the first distillation column.

7 . The method according to claim 1 , wherein the portion of the second fraction of the supply flow introduced into the second dynamic pressure reduction turbine is conveyed from a separation point of the supply flow to the second dynamic pressure reduction turbine without passing through any heat exchanger.

8 . The method according to claim 7 , wherein an entirety of the second fraction of the supply flow is introduced into the second dynamic pressure reduction turbine without cooling between the step of separating the supply flow and the step of introducing the second fraction of the supply flow into the second dynamic pressure reduction turbine.

9 . The method according to claim 1 , comprising:
removing a secondary compression fraction from the upper column flow rich in methane, before the upper column flow rich in methane is passed into the first compressor; passing the secondary compression fraction into a third compressor coupled to the second dynamic pressure reduction turbine; and introducing the compressed secondary compression fraction from the third compressor into the compressed upper column flow, downstream of the first compressor.

10 . The method according to claim 1 , comprising:
removing a make-up cooling flow from the upper column flow rich in methane or from a flow formed from the upper column flow rich in methane; and pressure reducing and introducing the make-up cooling flow subjected to pressure reduction into a flow flowing upstream of the first pressure reduction turbine.

11 . The method according to claim 1 , wherein the second compressor comprises a first compression stage, at least a second compression stage, and a cooler interposed between the first compression stage and the second compression stage, the method comprising:
passing the compressed upper column flow from the first compressor successively into the first compression stage, into the cooler, and then into the second compression stage.

12 . The method according to claim 1 , comprising pressure reducing and partially vaporizing the heavy lower flow in the first heat exchanger.

13 . The method according to claim 1 , comprising:
separating a third supply flow fraction from the supply flow, introducing the third supply flow fraction in an upstream heat exchanger, and cooling the third supply flow with flow issuing from the downstream heat exchanger.

14 . An installation for producing a flow rich in methane and a flow rich in C 2 + hydrocarbons from a supply flow containing hydrocarbons, the installation comprising:
a supply flow separator configured to separate the supply flow into a first fraction of the supply flow and at least a second fraction of the supply flow;
a first heat exchanger configured to cool the first fraction of the supply flow;
a first heat exchange introducer configured to introduce the first fraction of the supply flow into the first heat exchanger;
a first separation flask and a first separation flask introducer configured to introduce the cooled first fraction of the supply flow into the first separation flask in order to produce a light upper flow and a heavy lower flow;
a light upper flow divider configured to

Assignees

• Technip France

Inventors

• Gahier Vanessa
• Gouriou Julie
• Barthe Loic
• Thiebault Sandra

Classifications

• F25J3/0209 Primary

  Natural gas or substitute natural gas · CPC title

• F25J3/0233

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

• F25J3/0238

  separation of CnHm with 2 carbon atoms or more · CPC title

• F25J2200/02

  in a single pressure main column system · CPC title

• F25J2200/30

  using a side column in a single pressure column system · CPC title