-
公开(公告)号：US12122964B2
公开(公告)日：2024-10-22
申请号：US18208965
申请日：2023-06-13
Applicant: CONOCOPHILLIPS COMPANY
Inventor： Paul R. Davies , Michael J. Calderon , Dale L. Embry , David W. Larkin , Qi Ma
CPC classification number: C10G53/02 , B01D1/28 , B01D3/06 , B01D3/143 , C10G7/00 , B01D2256/24 , B01D2257/7022 , C10G2300/1025 , C10G2300/1081 , C10G2400/28
Abstract: The invention relates to various nonlimiting embodiments that include methods, apparatuses or systems for processing natural gas comprising a heavies removal column processing natural gas and light oil reflux. The overhead stream goes to heavies treated natural gas storage. The heavies removal column reboiler bottoms stream product is input to a debutanizer column. The debutanizer column overhead lights are input to a flash drum where the bottoms is pumped through a heat exchanger as a light oil reflux input to the heavies removal column, while the debutanizer reboiler bottoms product is stored as stabilized condensate. Alternatively, debutanizer column overhead lights are sent to heavies treated gas storage and the bottoms stream product goes to a depentanizer column, the overhead lights are pumped through a heat exchanger as a light oil reflux input to the heavies removal column, while the depentanizer reboiler bottoms product is stabilized condensate.
-
Patent Agency Ranking
公开(公告)号：US20240310118A1
公开(公告)日：2024-09-19
申请号：US18671297
申请日：2024-05-22
Applicant: ConocoPhillips Company
Inventor： Michael J. Calderon , Dale L. Embry , Paul R. Davies , Attilio J. Praderio
CPC classification number: F25J3/0295 , B01D53/1425 , B01D53/1431 , F25J3/0209 , F25J3/0247 , F25J2200/10 , F25J2210/04 , F25J2220/64
Abstract: Implementations described and claimed herein provide systems and methods for processing liquefied natural gas (LNG). In one implementation, a solvent is injected into a feed of natural gas at a solvent injection point. A mixed feed is produced from a dispersal of the solvent into the feed of natural gas. The mixed feed contains heavy components. A chilled feed is produced by chilling the mixed feed. The chilled feed includes a vapor and a condensed liquid. The condensed liquid contains a fouling portion of the heavy components condensed by the solvent during chilling. The liquid containing the fouling portion of the heavy components is separated from the vapor. The vapor is directed into a feed chiller heat exchanger following separation of the liquid containing the fouling portion of the heavy components from the vapor, such that the vapor being directed into feed chiller heat exchanger is free of freezing components.
-
公开(公告)号：US11713423B2
公开(公告)日：2023-08-01
申请号：US17247622
申请日：2020-12-18
Applicant: CONOCOPHILLIPS COMPANY
Inventor： Paul R. Davies , Michael J. Calderon , Dale L. Embry , David W. Larkin , Qi Ma
CPC classification number: C10G53/02 , B01D1/28 , B01D3/06 , B01D3/143 , C10G7/00 , B01D2256/24 , B01D2257/7022 , C10G2300/1025 , C10G2300/1081 , C10G2400/28
Abstract: The invention relates to various nonlimiting embodiments that include methods, apparatuses or systems for processing natural gas comprising a heavies removal column processing natural gas and light oil reflux. The overhead stream goes to heavies treated natural gas storage. The heavies removal column reboiler bottoms stream product is input to a debutanizer column. The debutanizer column overhead lights are input to a flash drum where the bottoms is pumped through a heat exchanger as a light oil reflux input to the heavies removal column, while the debutanizer reboiler bottoms product is stored as stabilized condensate. Alternatively, debutanizer column overhead lights are sent to heavies treated gas storage and the bottoms stream product goes to a depentanizer column, the overhead lights are pumped through a heat exchanger as a light oil reflux input to the heavies removal column, while the depentanizer reboiler bottoms product is stabilized condensate.
-
公开(公告)号：US20230194161A1
公开(公告)日：2023-06-22
申请号：US18109888
申请日：2023-02-15
Applicant: ConocoPhillips Company
Inventor： Jinghua Chan , Qi Ma , Dale L. Embry , Attilio J. Praderio
CPC classification number: F25J1/0022 , F25J1/0247 , F25J3/0209 , F25J3/0233 , F25J3/0242 , F25J3/0295 , F25J1/004 , F25J2270/60 , F25J2200/02 , F25J2200/76 , F25J2200/78 , F25J2205/02 , F25J2220/60 , F25J2220/64 , F25J2245/02 , F25J2270/12
Abstract: Implementations described and claimed herein provide systems and methods for processing liquefied natural gas (LNG). In one implementation, a dry feed gas is received. The dry feed gas is chilled with clean vapor from a heavies removal column to form a chilled feed gas. The chilled feed gas is partially condensed into a vapor phase and a liquid phase. The liquid phase retains freezing components. The freezing components are extracted using a reflux stream in the heavies removal column. The freezing components are removed as a condensate. The vapor phase is compressed into a clean feed gas. The clean feed gas is free of the freezing components for downstream liquefaction.
-
公开(公告)号：US11604025B2
公开(公告)日：2023-03-14
申请号：US17072565
申请日：2020-10-16
Applicant: ConocoPhillips Company
Inventor： Jinghua Chan , Qi Ma , Dale L. Embry , Attilio J. Praderio
Abstract: Implementations described and claimed herein provide systems and methods for processing liquefied natural gas (LNG). In one implementation, a dry feed gas is received. The dry feed gas is chilled with clean vapor from a heavies removal column to form a chilled feed gas. The chilled feed gas is partially condensed into a vapor phase and a liquid phase. The liquid phase retains freezing components. The freezing components are extracted using a reflux stream in the heavies removal column. The freezing components are removed as a condensate. The vapor phase is compressed into a clean feed gas. The clean feed gas is free of the freezing components for downstream liquefaction.
-
公开(公告)号：US20210116173A1
公开(公告)日：2021-04-22
申请号：US17072565
申请日：2020-10-16
Applicant: ConocoPhillips Company
Inventor： Jinghua Chan , Qi Ma , Dale L. Embry , Attilio J. Praderio
Abstract: Implementations described and claimed herein provide systems and methods for processing liquefied natural gas (LNG). In one implementation, a dry feed gas is received. The dry feed gas is chilled with clean vapor from a heavies removal column to form a chilled feed gas. The chilled feed gas is partially condensed into a vapor phase and a liquid phase. The liquid phase retains freezing components. The freezing components are extracted using a reflux stream in the heavies removal column. The freezing components are removed as a condensate. The vapor phase is compressed into a clean feed gas. The clean feed gas is free of the freezing components for downstream liquefaction.
-
-
-
-
-
Search Results
16
records
(took 0.039 seconds)
