Systems and methods for removing nitrogen during liquefaction of natural gas

Patent metadata

Field	Value
Publication number	US-12455114-B2
Application number	US-202017092518-A
Country	US
Kind code	B2
Filing date	Nov 9, 2020
Priority date	Nov 7, 2019
Publication date	Oct 28, 2025
Grant date	Oct 28, 2025

Abstract

Implementations described and claimed herein provide systems and methods for removing nitrogen during liquefaction of natural gas. In one implementation, a nitrogen rejection unit is used in an LNG facility to remove nitrogen from natural gas during an LNG liquefaction process. The nitrogen rejection unit contains at least two columns and at least one 3-stream condenser, 2-stream condenser or a two 2-stream condenser.

First claim

What is claimed is:

1. A method for removing nitrogen from a natural gas stream in a liquefied natural gas facility, the method comprising:
liquefying the natural gas stream at least partially in the liquefied natural gas facility to form a liquefied natural gas stream;
routing the liquefied natural gas stream through a nitrogen rejection unit, the nitrogen rejection unit including an upstream nitrogen removal column, a downstream nitrogen removal column, an intermediate nitrogen removal column, a first condenser, and a second condenser;
condensing a nitrogen-containing stream of the liquefied natural gas stream at least partially via indirect heat exchange using the first condenser and the second condenser, each of the first condenser and the second condenser being independently a 3-stream condenser or a 2-stream condenser, the nitrogen rejection unit removing nitrogen from the liquefied natural gas stream;
routing the liquefied natural gas stream to the upstream nitrogen removal column, where a first top stream and a first bottom stream form;
routing a first portion of the first top stream to the first condenser;
removing a second portion of the first top stream from the nitrogen rejection unit;
routing a third portion of the first top stream to the intermediate nitrogen removal column;
removing the first bottom stream from the nitrogen rejection unit, the first bottom stream removed from the nitrogen rejection unit containing heavies;
routing the first portion of the first top stream from the first condenser to the intermediate nitrogen removal column, where a second top stream and a second bottom stream are formed;
routing at least a portion of the second top stream to the second condenser before routing to the downstream nitrogen removal column;
forming a third top stream and a third bottom stream in the downstream nitrogen removal column, wherein the third top stream comprises predominantly nitrogen;
routing the third bottom stream to an expansion drum;
forming a liquid stream and a gas stream using the expansion drum;
routing the liquid stream to the first condenser, the first condenser warming the liquid stream to form a warmed liquid stream before exiting the nitrogen rejection unit; and
combining the gas stream with the warmed liquid stream.

2. The method of claim 1 , wherein each of the first condenser and the second condenser is independently selected from the group consisting of: core-in-shell exchanger, brazed aluminum heat exchanger, shell and tube exchanger, kettle exchanger, printed circuit heat exchanger, and any combination thereof.

3. The method of claim 1 ,
wherein the first portion of the first top stream is cooled by the first condenser;
wherein the at least a portion of the second top stream is cooled by the second condenser; and
wherein the method further comprises:
routing the second top stream towards a top of the downstream nitrogen removal column;
routing the second bottom stream to the downstream nitrogen removal column, wherein the second bottom stream is introduced towards a bottom of the downstream nitrogen removal column;
removing at least a portion of the third top stream from the nitrogen rejection unit; and
collecting at least a portion of the third bottom stream from the downstream nitrogen removal column, the third bottom stream comprising predominantly methane.

4. The method of claim 1 ,
wherein the first portion of the first top stream is at least partially condensed by the first condenser;
wherein the at least a portion of the second top stream is being condensed before routing to the downstream nitrogen removal column; and
wherein the method further comprises:
routing the second bottom stream to the second condenser before routing to the downstream nitrogen removal column;
routing at least a portion of the third top stream to the second condenser and then to the first condenser; and
routing the third bottom stream to the first condenser, the third bottom stream comprising methane.

5. The method of claim 1 , wherein the nitrogen rejection unit further comprises one or more reboilers, the one or more reboilers providing heating duty to one or more of the upstream, intermediate, and downstream nitrogen removal columns.

6. The method of claim 1 , wherein one or more of the upstream, intermediate, and downstream nitrogen removal columns provide a heating duty via a stripping gas or heating gas.

7. The method of claim 1 , wherein at least one of the first condenser or the second condenser is a printed circuit heat exchanger.

8. The method of claim 1 , wherein the first condenser and second condenser are 3-stream condensers; or the first condenser is the 3-stream condenser and the second condenser and a third condenser are the 2-stream condensers.

9. The method of claim 1 , wherein the natural gas stream from a main liquefaction process is a natural gas stream from a methane cold box of a main liquefaction process, the main liquefaction process including one or more refrigeration cycles external to the nitrogen rejection unit.

10. The method of claim 1 , wherein one or more of the upstream nitrogen removal column and the downstream nitrogen removal column includes a trap out tray, a chimney tray, or both.

11. The method of claim 4 , wherein the condensed second top stream is routed to a third condenser before it is routed to the downstream nitrogen removal column.

12. The method of claim 9 , wherein a bottom stream from the downstream nitrogen removal column is routed to the main liquefaction process.

13. A liquefied natural gas system comprising:
one or more refrigeration cycles successively cooling a fluid stream, each of the one or more refrigeration cycles including a refrigerant, a compressor, and a chiller;
an upstream nitrogen removal column of a nitrogen rejection unit wherein the upstream nitrogen removal column is operable to form a first top stream and a first bottom stream from a nitrogen-containing stream, the first bottom stream removed from the nitrogen rejection unit, and the first bottom stream removed from the nitrogen rejection unit containing heavies;
a downstream nitrogen removal column of the nitrogen rejection unit;
an intermediate nitrogen removal column of the nitrogen rejection unit disposed between the upstream nitrogen removal column and the downstream nitrogen removal column;
a first condenser of the nitrogen rejection unit, wherein a first portion of the first top stream is routed to the first condenser before being routed to the intermediate nitrogen removal column, a second portion of the first top stream is removed from the nitrogen rejection unit, and a third portion of the first top stream is routed to the intermediate nitrogen removal column, and wherein the intermediate nitrogen removal column is operable to form a second top stream and a second bottom stream;
a second condenser of the nitrogen rejection unit, wherein at least a portion of the second top stream is routed to the second condenser before routing to the downstream nitrogen removal column, and wherein the first condenser and second condenser at least partially condense the nitrogen-containing stream via indirect heat exchange, and each of the first condenser and the second condenser are independently a 3-stream condenser, or a 2-stream condenser; and
an expansion drum of the nitrogen rejection unit configured to receive a third bottom stream formed in the downstream nitrogen removal column, the expansion drum configured to form a liquid stream and a gas stream, the liquid stream routed to the first condenser, the first condenser warming the liquid stream before exiting the nitrogen re

Assignees

• Conocophillips Co

Inventors

• James Will T
• Gentry Matthew C
• Qualls Wesley R

Classifications

• F25J2210/62

  Liquefied natural gas [LNG]; Natural gas liquids [NGL]; Liquefied petroleum gas [LPG] · CPC title

• F25J2215/62

  Ethane or ethylene · CPC title

• F25J2215/60

  Methane · CPC title

• F25J2215/64

  Propane or propylene · CPC title

• F25J3/0615

  Liquefied natural gas · CPC title