US2022364005A1PendingUtilityA1
Lng process for variable pipeline gas composition
Est. expiryApr 19, 2037(~10.8 yrs left)· nominal 20-yr term from priority
F25J 2260/20C10L 2290/543F25J 3/0238F25J 2280/10F25J 2235/60C10G 5/06F25J 3/0233F25J 2210/04F25J 2245/02F25J 3/0242F25J 3/0209F25J 2200/04C10G 2300/1025F25J 2205/04C10L 3/101F25J 2280/02F25J 2290/60F25J 3/0295C10L 3/10C10L 2290/10C10L 2200/0415
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Claims
Abstract
The invention relates to a system, method and apparatus for processing natural gas in an LNG facility. A natural gas feed is introduced into a heavies removal unit. The heavies removal system includes a heavies removal column and a distillation column. The heavies removal column and the distillation column are connected via a purge/recovery line. One or more components of the natural gas feed is purged from the heavies removal column to the distillation column via the purge/recovery line to obtain a specified concentration or concentration range of heavy components feeding into the distillation column.
Claims
exact text as granted — not AI-modified1 . A method for processing natural gas in an LNG facility comprising:
introducing a natural gas feed to a heavies removal unit, wherein the heavies removal system includes a heavies removal column and a distillation column, wherein the heavies removal column and the distillation column are fluidly connected; and purging one or more components of the natural gas feed from the heavies removal column to a methane recycle stream via the purge/recovery line to obtain a specified concentration or concentration range of heavy components feeding into the distillation column.
2 . The method of claim 1 , wherein the distillation column is a high pressure demethanizer.
3 . The method of claim 1 , further comprising:
adjusting rate of the purging based in order to adjust flow rate to the distillation column.
4 . The method of claim 1 , wherein the LNG facility is configured for a cascade liquefaction process.
5 . The method of claim 1 , wherein the heavies removal column is downstream of the distillation column.
6 . The method of claim 1 , wherein the purging removes hydrocarbons having 6 or more carbons.
7 . A method for processing natural gas feed during natural gas liquefaction comprising:
introducing the natural gas feed into a heavies removal unit, wherein the heavies removal system includes a heavies removal column and a demethanizer, wherein the heavies removal column and the demethanizer are fluidly connected and wherein the heavies removal column is downstream of the demethanizer; determining composition of the natural gas feed before it is introduced into the demethanizer; and purging one or more heavy components of the natural gas feed from the heavies removal column to a methane recycle stream via the purge/recovery line to reduce or increase concentration of heavy components feeding into the demethanizer.
8 . The method of claim 7 , further comprising:
adjusting rate of the purging in order to adjust flow rate to the distillation column.
9 . The method of claim 7 , wherein the natural gas liquefaction is a cascade liquefaction process.
10 . The method of claim 7 , wherein at least three pure refrigerants are used in the cascade liquefaction process.
11 . The method of claim 10 , wherein the pure refrigerants include methane, ethane, ethylene, propane, or propylene.
12 . The method of claim 7 , wherein the heavy components comprise carbon molecules having 6 or more carbon atoms.Cited by (0)
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