Multiple pressure mixed refrigerant cooling process

    公开(公告)号:US10753676B2

    公开(公告)日:2020-08-25

    申请号:US15718068

    申请日:2017-09-28

    IPC分类号: F25J1/00 F25J1/02

    摘要: Systems and methods described for increasing capacity and efficiency of natural gas liquefaction processes having a mixed refrigerant precooling system with multiple pressure levels comprising cooling the compressed mixed refrigerant stream and separating the cooled compressed mixed refrigerant stream into a vapor and liquid portion. The liquid portion provides refrigeration duty to a first precooling heat exchanger. The vapor portion is further compressed, cooled, and condensed, and used to provide refrigeration duty to a second precooling heat exchanger. A flash gas separated from the liquefied natural gas is warmed and combined with the natural gas feed stream.

    Method and System for Cooling a Hydrocarbon Stream Using a Gas Phase Refrigerant

    公开(公告)号:US20190331413A1

    公开(公告)日:2019-10-31

    申请号:US15964302

    申请日:2018-04-27

    IPC分类号: F25J1/00 F25J1/02

    摘要: Described herein are methods and systems for the liquefaction of a natural gas stream using a refrigerant comprising methane or a mixture of methane and nitrogen. The methods and systems use a refrigeration circuit and cycle that employs one or more turbo-expanders to expand one or more streams of gaseous refrigerant to provide one or more streams of at least predominantly gaseous refrigerant that are used to provide refrigeration for liquefying and/or precooling the natural gas, and a J-T valve to expand down to a lower pressure a stream of liquid or two-phase refrigerant to provide a vaporizing stream of refrigerant that provides refrigeration for sub-cooling.

    MULTIPLE PRESSURE MIXED REFRIGERANT COOLING PROCESS AND SYSTEM

    公开(公告)号:US20180100694A1

    公开(公告)日:2018-04-12

    申请号:US15287963

    申请日:2016-10-07

    IPC分类号: F25J1/00 F25J1/02

    摘要: Systems and methods described for increasing capacity and efficiency of natural gas liquefaction processes having a mixed refrigerant precooling system with multiple pressure levels comprisingcooling the compressed mixed refrigerant stream and separating the cooled compressed mixed refrigerant stream into a vapor and liquid portion. The liquid portion provides refrigeration duty to a first precooling heat exchanger. The vapor portion is further compressed, cooled, and condensed, and used to provide refrigeration duty to a second precooling heat exchanger. Optionally additional precooling heat exchangers, and/or phase separators may be used.

    Refrigerant Recovery in Natural Gas Liquefaction Processes

    公开(公告)号:US20180058752A1

    公开(公告)日:2018-03-01

    申请号:US15671622

    申请日:2017-08-08

    IPC分类号: F25J1/00 F25J3/02 F25J1/02

    摘要: Described herein is a method of removing refrigerant from a natural gas liquefaction system in which vaporized mixed refrigerant is withdrawn from the closed-loop refrigeration circuit and introduced into a distillation column so as to be separated into an overhead vapor enriched in methane and a bottoms liquid enriched in heavier components. Overhead vapor is withdrawn from the distillation column to form a methane enriched stream that is removed from the liquefaction system, and bottoms liquid is reintroduced from the distillation column into the closed-loop refrigeration circuit. Also described are methods of altering the rate of production in a natural gas liquefaction system in which refrigerant is removed as described above, and a natural gas liquefaction systems in which such methods can be carried out.

    Method and system for cooling a hydrocarbon stream

    公开(公告)号:US11624555B2

    公开(公告)日:2023-04-11

    申请号:US16826907

    申请日:2020-03-23

    摘要: A system and method for increasing the efficiency of natural gas liquefaction processes by using a hybrid cooling system and method. More specifically, a system and method for converting a transcritical precooling refrigeration process to a subcritical process. In one embodiment, the refrigerant is cooled to sub-critical temperature using an economizer. In another embodiment, the refrigerant is cooled to a sub-critical temperature using an auxiliary heat exchanger. Optionally, the economizer or auxiliary heat exchanger can be bypassed when ambient temperatures are sufficiently low to cool the refrigerant to a sub-critical temperature. In another embodiment, the refrigerant is isentropically expanded.

    METHOD AND SYSTEM FOR COOLING A HYDROCARBON STREAM

    公开(公告)号:US20200217585A1

    公开(公告)日:2020-07-09

    申请号:US16826907

    申请日:2020-03-23

    摘要: A system and method for increasing the efficiency of natural gas liquefaction processes by using a hybrid cooling system and method. More specifically, a system and method for converting a transcritical precooling refrigeration process to a subcritical process. In one embodiment, the refrigerant is cooled to sub-critical temperature using an economizer. In another embodiment, the refrigerant is cooled to a sub-critical temperature using an auxiliary heat exchanger. Optionally, the economizer or auxiliary heat exchanger can be bypassed when ambient temperatures are sufficiently low to cool the refrigerant to a sub-critical temperature. In another embodiment, the refrigerant is isentropically expanded.

    Multiple pressure mixed refrigerant cooling process and system

    公开(公告)号:US10663220B2

    公开(公告)日:2020-05-26

    申请号:US15287963

    申请日:2016-10-07

    IPC分类号: F25J1/02 F25J1/00

    摘要: Systems and methods described for increasing capacity and efficiency of natural gas liquefaction processes having a mixed refrigerant precooling system with multiple pressure levels comprising cooling the compressed mixed refrigerant stream and separating the cooled compressed mixed refrigerant stream into a vapor and liquid portion. The liquid portion provides refrigeration duty to a first precooling heat exchanger. The vapor portion is further compressed, cooled, and condensed, and used to provide refrigeration duty to a second precooling heat exchanger. Optionally additional precooling heat exchangers, and/or phase separators may be used.