Back to results
US 2024/0125549 A1Published application
Open Loop Liquefaction Process with NGL Recovery
AssigneeAir Products and Chemicals, Inc.
InventorsMark Julian Roberts, Russell B. Shnitser, Christopher Michael Ott, Annemarie Ott Weist
Life of this patent
Estimating the term…
Abstract
Described herein are methods and systems for removing natural gas liquids from a natural gas feed stream and for liquefying the natural gas feed stream so as to produce a liquefied natural gas (LNG) stream and a natural gas liquids (NGL) stream
Claims20
A method for removing natural gas liquids from and liquefying a natural gas feed stream, the method comprising the steps of:
- (a) expanding and/or cooling a natural gas feed stream and introducing said stream into a distillation column having one or more separation sections, the natural gas feed stream being introduced into the distillation column below at least one of said separation sections;
- (b) withdrawing a natural gas liquids stream from the bottom of the distillation column;
- (c) withdrawing a natural gas vapor stream from the top of the distillation column
- (d) warming the natural gas vapor stream and a first expanded refrigerant stream in one or more heat exchanger sections, compressing the resulting warmed streams, and combining said streams to form a compressed refrigerant, wherein the natural gas vapor stream and first expanded refrigerant stream may be combined prior to, during or after being warmed and compressed;
- (e) cooling at least a first portion of the compressed refrigerant, via indirect heat exchange with the natural gas vapor stream and the first expanded refrigerant stream that are being warmed in step (d), to form a first cold refrigerant stream;
- (f) expanding the first cold refrigerant stream and separating said stream into vapor and liquid phases to form a first liquefied natural gas stream from the liquid phase and the first expanded refrigerant stream from the vapor phase;
- (g) forming a reflux stream and expanding and introducing the reflux stream into the top of the distillation column to provide reflux to the distillation column, wherein the reflux stream is formed from a portion of the first liquefied natural gas stream, a portion of the liquid phase separated in step (f), a portion of the first cold refrigerant stream withdrawn from said stream prior to said stream being separated in step (f), a further portion of the compressed refrigerant that has been cooled via indirect heat exchange with the natural gas vapor stream and the first expanded refrigerant stream that are being warmed in step (d), and/or a portion of a liquefied natural gas stream or liquefied natural gas product derived from the first liquefied natural gas stream.
4 more elements
A system for removing natural gas liquids from and liquefying a natural gas feed stream, the system comprising:
- one or more expansion devices and/or heat exchanger sections arranged and configured to expanding and/or cool a natural gas feed stream to form an expanded and/or cooled natural gas feed stream;
- a distillation column having one or more separation sections, the distillation column being arranged and configured to receive the expanded and/or cooled natural gas feed stream into the distillation column below at least one of said separation sections and separate expanded and/or cooled natural gas feed stream into a natural gas liquids stream withdrawn from the bottom of the distillation column and a natural gas vapor stream withdrawn from the top of the distillation column;
- one or more conduits, heat exchanger sections and compression stages arranged and configured to receive and warm the natural gas vapor stream and a first expanded refrigerant stream, compress the resulting warmed streams and combine said streams to form a compressed refrigerant, wherein the one or more conduits, heat exchanger sections and compression stages and may be arranged and configured such that the natural gas vapor stream and first expanded refrigerant stream are combined prior to, during or after being warmed and compressed;
- one or more conduits arranged and configured to pass at least a first portion of the compressed refrigerant through the one or more heat exchanger sections so as to cool the at least a first portion of the compressed refrigerant via indirect heat exchange with the natural gas vapor stream and the first expanded refrigerant stream to form a first cold refrigerant stream;
- one or more expansion and separation devices for expanding the first cold refrigerant stream and separating said stream into vapor and liquid phases to form a first liquefied natural gas stream from the liquid phase and the first expanded refrigerant stream from the vapor phase;
- and
- one or more conduits and expansion devices arranged and configured to receive a reflux stream and expand and introduce the reflux stream into the top of the distillation column to provide reflux to the distillation column, wherein the reflux stream is formed from a portion of the first liquefied natural gas stream, a portion of the liquid phase separated in step (f), a portion of the first cold refrigerant stream withdrawn from said stream prior to said stream being separated in step (f), a further portion of the compressed refrigerant that has been cooled via indirect heat exchange with the natural gas vapor stream and the first expanded refrigerant stream that are being warmed in step (d), and/or a portion of a liquefied natural gas stream or liquefied natural gas product derived from the first liquefied natural gas stream.
4 more elements
Dependencies are inferred from the claim text.