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公开(公告)号:US20240337441A1
公开(公告)日:2024-10-10
申请号:US18745178
申请日:2024-06-17
发明人: Michael J. Calderon , Will T. James , Dale L. Embry , Jinghua Chan , Qi Ma
CPC分类号: F25J1/0022 , F25J1/02 , F25J3/0233 , F25J3/0238 , F25J3/0247 , F25J3/08 , F25J2200/04 , F25J2200/72 , F25J2220/04
摘要: Disclosed herein are systems and processes for removing heavies during the liquefaction of a natural gas. The processes include dissolving the heavies in the natural gas by adding external natural gas liquid (NGL), followed by a staged removal of the natural gas liquid (NGL) and dissolved heavies.
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公开(公告)号:US20240200869A1
公开(公告)日:2024-06-20
申请号:US18592856
申请日:2024-03-01
IPC分类号: F25J3/02
CPC分类号: F25J3/0238 , F25J3/0209 , F25J3/0219 , F25J3/0242 , F25J3/0295 , F25J2200/02 , F25J2200/38 , F25J2200/70 , F25J2205/04 , F25J2210/12 , F25J2210/60 , F25J2215/62 , F25J2215/64 , F25J2240/02 , F25J2270/06
摘要: To provide a process for separating hydrocarbons capable of recovering ethane or propane, including improved cold heat recovery enabling a reduction in compressor power. A process for separating hydrocarbons, in which a residual gas enriched with methane or ethane and a heavy fraction enriched with a lower volatile hydrocarbon are separated, includes: a) partially condensing the feed gas by cooling using the residual gas and another refrigerant as a refrigerant, followed by vapor-liquid separation; b) depressurizing and supplying the liquid obtained from step (a) to the distillation column; c) expanding a part or all of the gas obtained from step (a) by an expander to cause partial condensation, followed by vapor-liquid separation; d) feeding the liquid obtained from step (c) to the distillation column after using it as the further refrigerant in step (a); e) feeding a part or all of the gas obtained from step (c) to the distillation column; and f) obtaining the residual gas from the top of the distillation column and the heavy fraction from the bottom of the distillation column.
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公开(公告)号:US20240191941A1
公开(公告)日:2024-06-13
申请号:US18530954
申请日:2023-12-06
申请人: UOP LLC
发明人: Glen John Pomorski , Kyle Cuellar , Joseph Edward Zimmermann , Dennis Robert Ladendorf , Michael R. Van de Cotte
IPC分类号: F25J3/02
CPC分类号: F25J3/0242 , F25J3/0219 , F25J3/0238 , F25J2200/06 , F25J2215/62 , F25J2215/64 , F25J2260/60 , F25J2270/14
摘要: An improved process and apparatus integrate a deethanizer column with a cryogenic heat exchanger by condensing the deethanizer column overhead with a refrigerant stream in a cryogenic heat exchanger. A refrigerant compressor may provide refrigerant to the deethanizer overhead cryogenic condenser and a main cryogenic heat exchanger. Expansion of the refrigerant may provide sufficient cooling duty in one or both cryogenic exchangers.
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公开(公告)号:US11650008B2
公开(公告)日:2023-05-16
申请号:US16635102
申请日:2018-09-05
申请人: LG CHEM, LTD.
发明人: Tae Woo Kim , Sung Kyu Lee , Inseop Kim , Joon Ho Shin
CPC分类号: F25J3/0219 , C07C4/04 , C10G9/00 , F17C7/04 , F25J3/0238 , C10G2300/1044 , F17C2221/035 , F25J2210/12 , F25J2210/62 , F25J2215/64
摘要: A method for vaporizing liquid propane to be supplied as a raw material to a naphtha cracking ractor. The method comprises: decompressing liquid propane to lower a vaporization point and vaporize at least a portion of the liquid propane; utilizing vaporization heat, generated during vaporization of the portion of liquid propane, as a refrigerant; compressing the vaporized propane gas to increase pressure of the propane gas and produce compressed propane gas; and preheating the compressed propane gas. By using this method, it is possible to reduce pressure of liquid propane to a significantly lower pressure than the related art method so that all the vaporization latent heat or vaporization heat included in liquid propane may be utilized as a refrigerant, while also reducing heat energy consumed in a preheat process before it is supplied to the naphtha cracking reactor.
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公开(公告)号:US11644235B2
公开(公告)日:2023-05-09
申请号:US17222327
申请日:2021-04-05
CPC分类号: F25J3/0209 , F25J1/0022 , F25J1/0037 , F25J1/0092 , F25J1/0238 , F25J1/0262 , F25J1/0291 , F25J3/0233 , F25J3/0238 , F25J3/0295 , F25J3/04787 , F25J3/04872 , F25J5/002 , F25J5/005 , F28D9/0006 , F25J3/0242 , F25J3/0247 , F25J2200/02 , F25J2200/70 , F25J2200/74 , F25J2205/04 , F25J2205/40 , F25J2205/50 , F25J2205/60 , F25J2210/06 , F25J2210/12 , F25J2210/60 , F25J2215/04 , F25J2215/60 , F25J2215/62 , F25J2215/64 , F25J2215/66 , F25J2220/68 , F25J2230/30 , F25J2230/32 , F25J2230/60 , F25J2240/02 , F25J2240/60 , F25J2245/02 , F25J2260/60 , F25J2270/12 , F25J2270/18 , F25J2270/60 , F25J2270/66 , F25J2270/902 , F25J2290/40 , F25J2290/80
摘要: This specification relates to operating industrial facilities, for example, crude oil refining facilities or other industrial facilities that include operating plants that process natural gas or recover natural gas liquids.
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公开(公告)号:US20190186830A1
公开(公告)日:2019-06-20
申请号:US16135933
申请日:2018-09-19
CPC分类号: F25J3/0209 , F25J1/0022 , F25J1/0037 , F25J1/0092 , F25J1/0238 , F25J1/0291 , F25J3/0233 , F25J3/0238 , F25J3/0242 , F25J3/0247 , F25J3/0295 , F25J3/04787 , F25J3/04872 , F25J5/005 , F25J2200/02 , F25J2200/70 , F25J2200/74 , F25J2205/04 , F25J2205/40 , F25J2205/50 , F25J2205/60 , F25J2210/06 , F25J2210/12 , F25J2210/60 , F25J2215/04 , F25J2215/60 , F25J2215/62 , F25J2215/64 , F25J2215/66 , F25J2220/68 , F25J2230/20 , F25J2230/30 , F25J2230/32 , F25J2230/60 , F25J2240/02 , F25J2240/60 , F25J2245/02 , F25J2260/60 , F25J2270/12 , F25J2270/18 , F25J2270/60 , F25J2270/66 , F25J2270/902 , F25J2290/40 , F25J2290/62 , F25J2290/80
摘要: This specification relates to operating industrial facilities, for example, crude oil refining facilities or other industrial facilities that include operating plants that process natural gas or recover natural gas liquids.
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公开(公告)号:US20190186825A1
公开(公告)日:2019-06-20
申请号:US16135865
申请日:2018-09-19
CPC分类号: F25J3/0209 , F25J1/0022 , F25J1/0037 , F25J1/0092 , F25J1/0238 , F25J1/0291 , F25J3/0233 , F25J3/0238 , F25J3/0242 , F25J3/0247 , F25J3/0295 , F25J3/04787 , F25J3/04872 , F25J5/005 , F25J2200/02 , F25J2200/70 , F25J2200/74 , F25J2205/04 , F25J2205/40 , F25J2205/50 , F25J2205/60 , F25J2210/06 , F25J2210/12 , F25J2210/60 , F25J2215/04 , F25J2215/60 , F25J2215/62 , F25J2215/64 , F25J2215/66 , F25J2220/68 , F25J2230/20 , F25J2230/30 , F25J2230/32 , F25J2230/60 , F25J2240/02 , F25J2240/60 , F25J2245/02 , F25J2260/60 , F25J2270/12 , F25J2270/18 , F25J2270/60 , F25J2270/66 , F25J2270/902 , F25J2290/40 , F25J2290/62 , F25J2290/80
摘要: This specification relates to operating industrial facilities, for example, crude oil refining facilities or other industrial facilities that include operating plants that process natural gas or recover natural gas liquids.
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公开(公告)号:US20190186824A1
公开(公告)日:2019-06-20
申请号:US16135837
申请日:2018-09-19
CPC分类号: F25J3/0209 , F25J1/0022 , F25J1/0037 , F25J1/0092 , F25J1/0238 , F25J1/0291 , F25J3/0233 , F25J3/0238 , F25J3/0242 , F25J3/0247 , F25J3/0295 , F25J3/04787 , F25J3/04872 , F25J5/005 , F25J2200/02 , F25J2200/70 , F25J2200/74 , F25J2205/04 , F25J2205/40 , F25J2205/50 , F25J2205/60 , F25J2210/06 , F25J2210/12 , F25J2210/60 , F25J2215/04 , F25J2215/60 , F25J2215/62 , F25J2215/64 , F25J2215/66 , F25J2220/68 , F25J2230/20 , F25J2230/30 , F25J2230/32 , F25J2230/60 , F25J2240/02 , F25J2240/60 , F25J2245/02 , F25J2260/60 , F25J2270/12 , F25J2270/18 , F25J2270/60 , F25J2270/66 , F25J2270/902 , F25J2290/40 , F25J2290/62 , F25J2290/80
摘要: This specification relates to operating industrial facilities, for example, crude oil refining facilities or other industrial facilities that include operating plants that process natural gas or recover natural gas liquids.
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公开(公告)号:US20190186822A1
公开(公告)日:2019-06-20
申请号:US16135797
申请日:2018-09-19
CPC分类号: F25J3/0209 , F25J1/0022 , F25J1/0037 , F25J1/0092 , F25J1/0238 , F25J1/0291 , F25J3/0233 , F25J3/0238 , F25J3/0242 , F25J3/0247 , F25J3/0295 , F25J3/04787 , F25J3/04872 , F25J5/005 , F25J2200/02 , F25J2200/70 , F25J2200/74 , F25J2205/04 , F25J2205/40 , F25J2205/50 , F25J2205/60 , F25J2210/06 , F25J2210/12 , F25J2210/60 , F25J2215/04 , F25J2215/60 , F25J2215/62 , F25J2215/64 , F25J2215/66 , F25J2220/68 , F25J2230/20 , F25J2230/30 , F25J2230/32 , F25J2230/60 , F25J2240/02 , F25J2240/60 , F25J2245/02 , F25J2260/60 , F25J2270/12 , F25J2270/18 , F25J2270/60 , F25J2270/66 , F25J2270/902 , F25J2290/40 , F25J2290/62 , F25J2290/80
摘要: This specification relates to operating industrial facilities, for example, crude oil refining facilities or other industrial facilities that include operating plants that process natural gas or recover natural gas liquids.
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10.
公开(公告)号:US20190048754A1
公开(公告)日:2019-02-14
申请号:US15842213
申请日:2017-12-14
CPC分类号: F01K27/02 , B01D1/0058 , B01D1/0082 , B01D1/26 , B01D3/065 , B01D3/146 , B01D53/002 , B01D53/1456 , B01D53/263 , C02F1/16 , C02F2103/08 , C10G5/06 , C10G7/00 , F25B27/02 , F25J3/0209 , F25J3/0233 , F25J3/0238 , F25J3/0242 , F25J2200/02 , F25J2200/70 , F25J2200/74 , F25J2215/62 , F25J2240/70 , F25J2260/02 , F25J2270/12 , F25J2270/60 , F28D21/0001 , F28D2021/0019
摘要: Certain aspects of a natural gas liquid fractionation plant waste heat conversion to potable water using modified multi-effect distillation system can be implemented as a system that includes a waste heat recovery heat exchanger network thermally coupled to multiple heat sources of a Natural Gas Liquid (NGL) fractionation plant. The heat exchanger network is configured to recover at least a portion of heat generated at the multiple heat sources. The system includes a sub-system thermally coupled to the waste heat recovery heat exchanger network to receive at least a portion of heat recovered by the heat exchanger network. The sub-system is configured to perform one or more operations using at least the portion of heat recovered by the heat exchanger network.
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