Primary loop start-up method for a high pressure expander process

Patent metadata

Field	Value
Publication number	US-11635252-B2
Application number	US-201916526446-A
Country	US
Kind code	B2
Filing date	Jul 30, 2019
Priority date	Aug 22, 2018
Publication date	Apr 25, 2023
Grant date	Apr 25, 2023

Abstract

A method is disclosed for start-up of a system for liquefying a feed gas stream comprising natural gas. The system has a feed gas compression and expansion loop, and a refrigerant system comprising a primary cooling loop and a sub-cooling loop. The feed gas compression and expansion loop is started up. The refrigerant system is pressurized. Circulation in the primary cooling loop is started and established. Circulation in the sub-cooling loop is started and established. A flow rate of the feed gas stream and circulation rates of the primary cooling loop and the sub-cooling loop are ramped up.

First claim

What is claimed is:

1. A method for start-up of a system for liquefying a feed gas stream comprising natural gas, the system having a refrigerant system comprising a primary cooling loop and a sub-cooling loop, the method comprising:
(a) pressurizing the refrigerant system,

wherein step (a) comprises:
a1. providing the feed gas stream at a pressure less than 1,200 psia, and introducing a first portion of the feed gas stream to the primary cooling loop as a primary loop refrigerant;
a2. pressurizing a sub-cooling refrigerant in the sub-cooling loop to a sub-cooling loop pre-circulation pressure; and
a3. pressurizing the first portion of the feed gas stream in the primary cooling loop to a primary cooling loop pre-circulation pressure;
(b) starting and establishing circulation of the primary loop refrigerant in the primary cooling loop, the primary loop refrigerant passing through at least one primary cooling loop compressor unit and reaching a primary cooling loop discharge pressure that is higher than the primary cooling loop pre-circulation pressure;
(c) starting and establishing circulation of the sub-cooling refrigerant in the sub-cooling loop, the sub-cooling refrigerant passing through a sub-cooling loop compressor unit and reaching a sub-cooling loop discharge pressure that is higher than the sub-cooling cooling loop pre-circulation pressure; and
(d) after starting and establishing circulation in the primary cooling loop and in the sub-cooling loop, ramping up a flow rate of the first portion of the feed gas stream to the primary cooling loop and ramping up circulation rates within the primary cooling loop and the sub-cooling loop;
wherein a second portion of the feed gas stream undergoes indirect heat exchange with the primary loop refrigerant and the sub-cooling refrigerant in a heat exchanger zone.

2. The method of claim 1 , wherein the sub-cooling refrigerant comprises nitrogen.

3. The method of claim 1 , wherein step (c) comprises:
c1. starting the sub-cooling loop compressor unit with full recycle through an associated anti-surge valve (ASV);
c2. routing the sub-cooling refrigerant in the sub-cooling loop to a first heat exchanger within the heat exchanger zone to warm at least part of the primary loop refrigerant circulating in the primary cooling loop, thereby forming a cooled sub-cooling refrigerant;
c3. depressurizing and chilling the cooled sub-cooling refrigerant to form an expanded sub-cooling refrigerant;
c4. passing the expanded sub-cooling refrigerant sequentially to a second heat exchanger and the first heat exchanger within the heat exchanger zone to cool the second portion of the feed gas stream by indirect heat exchange, thereby forming a warmed sub-cooling refrigerant and a sub-cooled feed gas stream;
c5. compressing the warmed sub-cooling refrigerant in the sub-cooling loop compressor unit to produce a compressed sub-cooling loop refrigerant;
c6. increasing the discharge pressure of the sub-cooling loop compressor unit;
c7. adding further sub-cooling refrigerant to the sub-cooling loop while establishing circulation of the sub-cooling refrigerant in the sub-cooling loop;
c8. starting companders in the sub-cooling loop when a circulation rate within the sub-cooling loop reaches a required flow for compander operation; and
c9. establishing steady state operation of the system after ramping up the circulation rate of the primary loop refrigerant and the circulation rate of the sub-cooling loop refrigerant.

Assignees

• Liu Yijun
• Pierre Jr Fritz
• Nagavarapu Ananda K
• Wright Xiaoli Y
• Exxonmobil Technology & Engineering Company

Inventors

• Liu Yijun
• Pierre Jr Fritz
• Nagavarapu Ananda K
• Wright Xiaoli Y

Classifications

• F25J2230/30

  Compression of the feed stream · CPC title

• F25J2270/90

  External refrigeration, e.g. conventional closed-loop mechanical refrigeration unit using Freon or NH3, unspecified external refrigeration · CPC title

• F25J1/0037

  of a return stream · CPC title

• F25J1/0042

  by liquid expansion with extraction of work · CPC title

• F25J1/0082

  Methane · CPC title