Integrated nitrogen removal in the production of liquefied natural gas using refrigerated heat pump

Patent metadata

Field	Value
Publication number	US-9945604-B2
Application number	US-201414260753-A
Country	US
Kind code	B2
Filing date	Apr 24, 2014
Priority date	Apr 24, 2014
Publication date	Apr 17, 2018
Grant date	Apr 17, 2018

Abstract

A method for liquefying a natural gas feed stream and removing nitrogen therefrom, the method comprising passing a natural gas feed stream through a main heat exchanger to produce a first LNG stream, and separating a liquefied or partially liquefied natural gas stream in a distillation column to form nitrogen-rich vapor product, wherein a closed loop refrigeration system provides refrigeration to the main heat exchanger and to a condenser heat exchanger that provides reflux to the distillation column.

First claim

The invention claimed is:

1. A method for liquefying a natural gas feed stream and removing nitrogen therefrom, the method comprising:
(a) passing a natural gas feed stream through a main heat exchanger to cool and liquefy all or a portion of the natural gas stream, thereby producing a first LNG stream;
(b) withdrawing the first LNG stream from the main heat exchanger;
(c) expanding and partially vaporizing the first LNG stream, and introducing the expanded and partially vaporized LNG stream into a distillation column where the expanded and partially vaporized LNG stream is separated into a distillation column overhead vapor product stream and a distillation column liquid product stream, wherein the composition of the distillation column overhead vapor product stream is at least 99% mole fraction nitrogen;
(d1) providing reflux to the distillation column through a nitrogen heat pump by warming the distillation column overhead vapor product stream in a condenser heat exchanger to produce a warmed overhead vapor;
(d2) dividing the warmed overhead vapor into a first portion warmed overhead vapor and a second portion warmed overhead vapor;
(d3) compressing the first portion of the warmed overhead vapor to produce a compressed overhead vapor;
(d4) cooling the compressed overhead vapor in an ambient heat exchanger to produce a cooled compressed overhead stream;
(d5) further cooling and condensing the cooled compressed overhead stream in the condenser heat exchanger against first the distillation column overhead vapor product stream of step (d1) and then subsequently both the distillation column overhead vapor product stream of step (d1) and a closed loop refrigeration system to produce a condensed overhead vapor;
(d6) expanding the condensed overhead vapor and reintroducing the condensed overhead vapor back into the top of the distillation column as reflux stream;
(e) withdrawing the second portion of the warmed overhead vapor to form a nitrogen rich vapor product; and
(f) forming a second LNG stream from the distillation column liquid product stream withdrawn from the distillation column;
wherein refrigeration for the main heat exchanger is provided by the closed loop refrigeration system having refrigerant circulated and passing through and being warmed in the main heat exchanger and passing through and being warmed in the condenser heat exchanger.

2. The method of claim 1 , wherein the refrigerant that passes through and is warmed in the condenser heat exchanger is then passed through and further warmed in the main heat exchanger.

3. The method of claim 1 , wherein the warmed refrigerant, that is obtained after refrigeration has been provided to the main heat exchanger and to the condenser heat exchanger, is compressed in one or more compressors and cooled in one or more aftercoolers to form compressed refrigerant; the compressed refrigerant is passed through and cooled in the main heat exchanger to form cooled compressed refrigerant that is withdrawn from the main heat exchanger; and the cooled compressed refrigerant is then divided, with part of the refrigerant being expanded and returned directly to the main heat exchanger to pass through and be warmed in the main heat exchanger, and with another part of the refrigerant being expanded and sent to the condenser heat exchanger to pass through and be warmed in the condenser heat exchanger.

4. The method of claim 1 , wherein the refrigerant circulated by the closed loop refrigeration system is a mixed refrigerant.

5. The method of claim 4 , wherein the warmed mixed refrigerant, that is obtained after refrigeration has been provided to the main heat exchanger and to the condenser heat exchanger, is compressed, cooled in the main heat exchanger and separated as it the warmed mixed refrigerant is cooled so as to provide a plurality of liquefied or partially liquefied cold refrigerant streams of different compositions, the cold refrigerant stream with the highest concentration of lighter components obtained from the cold end of the main heat exchanger being divided and expanded so as to provide a stream of refrigerant that is warmed in the condenser heat exchanger and a stream of refrigerant that is returned to the cold end of the main heat exchanger to be warmed therein.

6. The method of claim 1 , wherein the method further comprises sending the second LNG stream to an LNG storage tank.

7. The method of claim 1 , wherein step (c) comprises expanding and partially vaporizing an at least partially liquefied nitrogen-enriched natural gas stream and introducing said stream into the distillation column to separate the stream into vapor and liquid phases, wherein the at least partially liquefied nitrogen-enriched natural gas stream is formed from separating a nitrogen-enriched natural gas stream from the first LNG stream and at least partially liquefying said stream in the main heat exchanger.

8. The method of claim 7 , wherein the least partially liquefied nitrogen-enriched natural gas stream is formed by (i) expanding, partially vaporizing and separating the first LNG stream, or an LNG stream formed from part of the first LNG stream, to form a nitrogen-depleted LNG product and a recycle stream composed of nitrogen-enriched natural gas vapor, (ii) compressing the recycle stream to form a compressed recycle stream, and (iii) passing the compressed recycle stream through the main heat exchanger, separately from and in parallel with the natural gas feed stream, to cool the compressed recycle stream and at least partially liquefy all or a portion thereof, thereby producing the at least partially liquefied nitrogen-enriched natural gas stream.

9. The method of claim 8 , wherein the first LNG stream, or the LNG stream formed from part of the first LNG stream, is expanded and transferred into an LNG storage tank in which a portion of the LNG vaporizes, thereby forming a nitrogen-enriched natural gas vapor and the nitrogen-depleted LNG product, and nitrogen-enriched natural gas vapor is withdrawn from the tank to form the recycle stream.

10. The method of claim 8 , wherein the method further comprises expanding, partially vaporizing and separating the second LNG stream to produce additional nitrogen-enriched natural gas vapor for the recycle stream and additional nitrogen-depleted LNG product.

11. The method of claim 1 , wherein step (c) comprises expanding and partially vaporizing an at least partially liquefied nitrogen-enriched natural gas stream and introducing said stream into the distillation column to separate the stream into vapor and liquid phases, wherein the at least partially liquefied nitrogen-enriched natural gas stream is formed from separating a nitrogen-enriched natural gas stream from the natural gas feed stream and at least partially liquefying said stream in the main heat exchanger.

12. The method of claim 11 , wherein step (a) comprises (i) introducing the natural gas feed stream into the warm end of the main heat exchanger, cooling and at least partially liquefying the natural gas feed stream, and withdrawing the cooled and at least partially liquefied stream from an intermediate location of the main heat exchanger, (ii) expanding, partially vaporizing and separating the cooled and at least partially liquefied stream to form a nitrogen-enriched natural gas vapor stream and a nitrogen-depleted natural gas liquid stream, and (iii) separately re-introducing the vapor and liquid streams into an intermediate location of the main heat exchanger and further cooling the vapor stream and liquid streams in parallel, the liquid stream being further cooled to form the first LNG stream and the vapor stream being further cooled and at least part

Assignees

• Air Prod & Chem

Inventors

• Ott Christopher Michael
• Krishnamurthy Gowri
• Chen Fei
• Liu Yang
• Roberts Mark Julian

Classifications

• F25J1/0042

  by liquid expansion with extraction of work · CPC title

• F25J3/0209

  Natural gas or substitute natural gas · CPC title

• F25J1/0022

  Hydrocarbons, e.g. natural gas · CPC title

• F25J1/0212

  as a single flow MCR cycle · CPC title

• F25J1/0025

  Boil-off gases "BOG" from storages · CPC title