Two-stage heavies removal in lng processing
AssigneeConocoPhillips Company
InventorsJinghua Chan, Paul R. Davies, Qi Ma, Michael J. Calderon, Dale L. Embry
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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.
Claims14
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.
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.
Dependencies are inferred from the claim text.