Two-stage heavies removal in lng processing

Patent metadata

Field	Value
Publication number	US-12111101-B2
Application number	US-202016893992-A
Country	US
Kind code	B2
Filing date	Jun 5, 2020
Priority date	Jun 5, 2019
Publication date	Oct 8, 2024
Grant date	Oct 8, 2024

Abstract

Implementations described and claimed herein provide systems and methods for processing liquefied natural gas (LNG). In one implementation, a feed gas is received and partially condensed into a two-phase stream by expanding the feed gas. A liquid containing fouling components is removed from the two-phase stream. A vapor generated from the two-phase stream is compressed into a compressed feed gas. The compressed feed gas is directed into a feed chiller heat exchanger. The compressed feed gas is free of the fouling components.

First claim

What is claimed is:

1. A method for reducing fouling in a liquefied natural gas (LNG) facility, the method comprising:
receiving a feed gas;
partially condensing the feed gas into a two-phase stream by expanding the feed gas, wherein the two-phase stream includes a liquid that includes fouling components, the fouling components including C12-C16 hydrocarbons;
separating the two-phase stream into a liquid stream and a gas stream in an expander outlet separator, the liquid stream including light components;
partially vaporizing the light components in a expander outlet separator heater from the liquid stream to form a vapor stream, the vapor stream directed from an outlet of the expander outlet separator heater into an inlet of an upper section of the expander outlet separator for joining with the gas stream for output as a vapor, any remaining liquid from the liquid stream directed from the expander outlet separator heater into a lower section of the expander outlet separator for joining a liquid accumulation for removal as the liquid containing the fouling components;
compressing the vapor output from the expander outlet separator into a compressed feed gas; and
directing the compressed feed gas into a feed chiller heat exchanger, the compressed feed gas free of the fouling components.

2. The method of claim 1 , wherein the feed gas is injected with bottoms liquid from a heavies removal column.

3. The method of claim 2 , wherein the bottoms liquid is vaporized and dispersed in the feed gas.

4. The method of claim 1 , further comprising:
removing heavy components from the compressed feed gas using a heavies removal column following chilling with the feed chiller heat exchanger.

5. The method of claim 1 , wherein the feed gas is isentropically expanded such that the two-phase stream is an isentropically expanded stream.

6. The method of claim 5 , wherein the liquid that includes the fouling components is removed from the feed gas in a first stage of removal.

7. The method of claim 6 , wherein the isentropically expanded stream is formed by a feed gas expander of a heavies pre-removal section isentropically expanding the feed gas.

8. The method of claim 7 , wherein compressing the vapor from the two-phase stream into the compressed feed gas is performed by a feed gas re-compressor of the heavies pre-removal section.

9. The method of claim 5 , further comprising:
chilling the compressed feed gas using the feed chiller heat exchanger.

10. The method of claim 9 , further comprising:
removing heavy components from the chilled feed in a second stage of removal.

11. The method of claim 1 , wherein expanding the feed gas includes partially condensing the feed gas through isentropic expansion.

12. A system for reducing fouling in a liquefied natural gas (LNG) facility, the system comprising:
a feed gas expander configured to receive a feed gas, the feed gas expander configured to partially condense the feed gas into a two-phase stream by expanding the feed gas, wherein the two-phase stream includes a liquid that includes fouling components, the fouling components including C12-C16 hydrocarbons;
an expander outlet separator configured to separate the two-phase stream into a liquid stream and a gas stream, the liquid stream including light components;
an expander outlet separator heater configured to partially vaporize light components from the liquid stream to form a vapor stream, the vapor stream directed from an outlet of the expander outlet separator heater into an inlet of an upper section of the expander outlet separator for joining with the gas stream for output as a vapor, any remaining liquid from the liquid stream configured to be directed from the expander outlet separator heater into a lower section of the expander outlet separator for joining a liquid accumulation for removal as the liquid containing the fouling components; and
a feed gas re-compressor configured to compress the vapor output from the expander outlet separator into a compressed feed gas, the compressed feed gas configured to be directed into a feed chiller heat exchanger, the compressed feed gas free of the fouling components.

13. The system of claim 12 , further comprising:
an expander suction scrubber, the feed gas configured to flow through the expander suction scrubber prior to entering the feed gas expander.

14. The system of claim 12 , wherein the feed gas is configured to be injected with bottoms liquid from a heavies removal column.

Assignees

• Conocophillips Co

Inventors

• Chan Jinghua
• Davies Paul R
• Ma Qi
• Calderon Michael J
• Embry Dale L

Classifications

• F25J2205/10

  using combined expansion and separation, e.g. in a vortex tube, "Ranque tube" or a "cyclonic fluid separator", i.e. combination of an isentropic nozzle and a cyclonic separator; Centrifugal separation · CPC title

• F25J2205/02

  using simple phase separation in a vessel or drum · CPC title

• F25J2215/60

  Methane · CPC title

• F25J2220/64

  Separating heavy hydrocarbons, e.g. NGL, LPG, C4+ hydrocarbons or heavy condensates in general · CPC title

• F25J3/0238

  separation of CnHm with 2 carbon atoms or more · CPC title