Refrigerant recovery in natural gas liquefaction processes

Patent metadata

Field	Value
Publication number	US-9759480-B2
Application number	US-201414511774-A
Country	US
Kind code	B2
Filing date	Oct 10, 2014
Priority date	Oct 10, 2014
Publication date	Sep 12, 2017
Grant date	Sep 12, 2017

Abstract

Described herein is a method of removing refrigerant from a natural gas liquefaction system in which vaporized mixed refrigerant is withdrawn from the closed-loop refrigeration circuit and introduced into a distillation column so as to be separated into an overhead vapor enriched in methane and a bottoms liquid enriched in heavier components. Overhead vapor is withdrawn from the distillation column to form a methane enriched stream that is removed from the liquefaction system, and bottoms liquid is reintroduced from the distillation column into the closed-loop refrigeration circuit. Also described are methods of altering the rate of production in a natural gas liquefaction system in which refrigerant is removed as described above, and a natural gas liquefaction systems in which such methods can be carried out.

First claim

The invention claimed is:

1. A method of altering the rate of production of liquefied or subcooled natural gas in a natural gas liquefaction system that uses a mixed refrigerant to liquefy and/or subcool the natural gas, the liquefaction system comprising a closed-loop refrigeration circuit in which the mixed refrigerant is circulated, the mixed refrigerant comprising a mixture of methane and one or more heavier components, and the closed-loop refrigeration circuit including a main heat exchanger through which natural gas is fed to be liquefied and/or subcooled by indirect heat exchange with the circulating mixed refrigerant, the method comprising:
a first period of time during which natural gas is fed through the main heat exchanger at a first feed rate and mixed refrigerant is circulated in the closed-loop refrigeration circuit at a first circulation rate so as to produce liquefied or subcooled natural gas at a first production rate;
a second period of time during which the production of liquefied or subcooled natural gas is stopped, or the rate of production of liquefied or subcooled natural gas is reduced, relative to the first production rate, to a second production rate, by stopping the feed of natural gas through the main heat exchanger or reducing the feed rate thereof to a second feed rate, stopping the circulation of the mixed refrigerant in the closed-loop refrigeration circuit or reducing the circulation rate thereof to a second circulation rate, and removing refrigerant from the liquefaction system, wherein the removing refrigerant from the liquefaction system comprises:
(a) withdrawing vaporized mixed refrigerant from the closed-loop refrigeration circuit;
(b) introducing the vaporized mixed refrigerant into a distillation column and providing reflux to the distillation column so as to separate the vaporized mixed refrigerant into an overhead vapor enriched in methane and bottoms liquid enriched in heavier components, wherein the overhead vapor is enriched in methane relative to the bottoms liquid, and the bottoms liquid is enriched in heavier components relative to the overhead vapor;
(c) withdrawing overhead vapor from the distillation column to form a methane enriched stream that is removed from the liquefaction system; and
(d) reintroducing bottoms liquid from the distillation column into the closed-loop refrigeration circuit, and/or storing bottoms liquid such that it can subsequently be reintroduced into the closed-loop refrigeration circuit.

2. The method of claim 1 , wherein the method further comprises, after the second period of time:
a third period of time during which the rate of production of liquefied or subcooled natural gas is increased to a third production rate, by increasing the feed of natural gas through the main heat exchanger to a third feed rate, adding refrigerant to the liquefaction system, and increasing the circulation of the mixed refrigerant to a third circulation rate, wherein the step of adding refrigerant to the liquefaction system comprises introducing methane into the closed-loop refrigeration circuit and, if bottoms liquid has not already been reintroduced into the closed-loop refrigeration circuit in step (d) of the second time period, reintroducing stored bottoms liquid into the closed-loop refrigeration circuit.

3. The method of claim 2 , wherein the third production rate of liquefied or subcooled natural gas, third feed rate of natural gas and third circulation rate of mixed refrigerant are the same as or less than the first production rate, first feed rate and first circulation rate, respectively.

4. The method of claim 2 , wherein the methane that is introduced into the closed-loop refrigeration circuit is obtained from the natural gas supply that provides natural gas for liquefaction in the liquefaction system.

Assignees

• Air Prod & Chem

Inventors

• Johnson Brian Keith
• Krishnamurthy Gowri
• Roberts Mark Julian

Classifications

• F25J1/0249

  Controlling refrigerant inventory, i.e. composition or quantity (charging or discharging refrigerants in cooling systems F25B45/00) · CPC title

• F25J1/0092

  Mixtures of hydrocarbons comprising possibly also minor amounts of nitrogen · CPC title

• F25J1/0055

  originating from an incorporated cascade · CPC title

• F25J2200/02

  in a single pressure main column system · CPC title

• F25J1/0022 Primary

  Hydrocarbons, e.g. natural gas · CPC title