Method and system for liquefaction of natural gas using liquid nitrogen

Patent metadata

Field	Value
Publication number	US-11079176-B2
Application number	US-201916262243-A
Country	US
Kind code	B2
Filing date	Jan 30, 2019
Priority date	Mar 14, 2018
Publication date	Aug 3, 2021
Grant date	Aug 3, 2021

Abstract

A method for producing liquefied natural gas (LNG) from a natural gas stream having a nitrogen concentration of greater than 1 mol %. At least one liquid nitrogen (LIN) stream is received at an LNG liquefaction facility. The LIN streams may be produced at a different geographic location from the LNG liquefaction facility. A natural gas stream is liquefied by indirect heat exchange with a nitrogen vent stream to form a pressurized LNG stream. The pressurized LNG stream has a nitrogen concentration of greater than 1 mol %. The pressurized LNG stream is directed to one or more stages of a column to produce an LNG stream and the nitrogen vent stream. The column has upper stages and lower stages. The LIN streams are directed to one or more upper stages of the column.

First claim

What is claimed is:

1. A method for producing liquefied natural gas (LNG) from a natural gas stream having a nitrogen concentration of greater than 1 mol %, where the method comprises:
at an LNG liquefaction facility, receiving a first liquefied nitrogen (LIN) stream and a second LIN stream, the first and second LIN streams being produced at a different geographical location than the LNG liquefaction facility;
liquefying the natural gas stream by indirect heat exchange with a nitrogen vent stream and the second liquefied nitrogen stream to form a pressurized LNG stream, where the pressurized LNG stream has a nitrogen concentration of greater than 1 mol %;
directing the pressurized LNG stream to a jet pump, and using the pressurized LNG stream as a motive fluid for the jet pump;
mixing the pressurized LNG stream and a lower pressure natural gas stream in the jet pump to produce a two-phase LNG stream, wherein the lower pressure natural gas stream has a pressure that is lower than a pressure of the pressurized LNG stream;
separating the two-phase LNG stream into an LNG vapor stream and an LNG liquid stream;
directing the LNG liquid stream to one or more stages of a column, wherein the column is one of a fractionation column, a distillation column, or an absorption column;
directing the LNG vapor stream to one or more lower stages of the column;
directing the first liquefied nitrogen stream to one or more upper stages of the column; and
producing an LNG stream and the nitrogen vent stream from the column.

2. The method of claim 1 , wherein the lower pressure natural gas stream comprises one of
boil-off gas extracted from LNG storage tanks, or boil-off gas extracted from LNG during storage or unloading operations from an LNG carrier ship.

3. The method of claim 1 , further comprising compressing the lower pressure natural gas stream prior to being directed to the column.

4. The method of claim 1 , further comprising:
indirectly exchanging heat between the nitrogen vent stream and the natural gas stream to form a warmed nitrogen vent stream.

5. The method of claim 1 , wherein the LNG stream has a nitrogen molar concentration of less than 1 mol %.

6. A method for producing liquefied natural gas (LNG) from a natural gas stream having a nitrogen concentration of greater than 1 mol %, where the method comprises:
at an LNG liquefaction facility, receiving one or more liquefied nitrogen (LIN) streams, the one or more LIN streams being produced at a different geographical location than the LNG liquefaction facility;
at least partially liquefying the natural gas stream by indirect heat exchange with a nitrogen vent stream to form a pressurized LNG stream, where the pressurized LNG stream has a nitrogen concentration of greater than 1 mol %;
directing the pressurized LNG stream to a separation vessel to produce an LNG vapor stream and an LNG liquid stream;
directing the LNG vapor stream to a jet pump, and using the LNG vapor stream as a motive fluid for the jet pump;
mixing the LNG vapor stream and a first lower pressure natural gas stream in the jet pump to produce a second lower pressure gas stream, wherein each of the first and second lower pressure natural gas streams have a pressure that is lower than a pressure of the pressurized LNG stream;
directing the LNG liquid stream to one or more stages of a column;
directing the second lower pressure natural gas stream to one or more lower stages of the column;
directing the one or more LIN streams to one or more upper stages of the column; and
producing an LNG stream and the nitrogen vent stream from the column.

7. The method of claim 6 , wherein the lower pressure natural gas stream comprises one of
boil-off gas extracted from LNG storage tanks, or
boil-off gas extracted from LNG during storage or unloading operations from an LNG carrier ship.

Assignees

• Pierre Jr Fritz
• Exxonmobil Upstream Res Co

Inventors

• Pierre Jr Fritz

Classifications

• F25J2210/04

  Mixing or blending of fluids with the feed stream · CPC title

• F25J2210/02

  Multiple feed streams, e.g. originating from different sources · CPC title

• F25J2205/30

  using a washing, e.g. "scrubbing" or bubble column for purification purposes · CPC title

• F25J2210/42

  Nitrogen · CPC title

• F25J1/0221

  using the cold stored in an external cryogenic component in an open refrigeration loop · CPC title