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41.发明授权Frigorific separation process of gas mixture by liquefying and rectifying 失效通过液化和整流进行气体混合物的冷冻分离过程
公开(公告)号：US2765637A
公开(公告)日：1956-10-09
申请号：US25063051
申请日：1951-10-10
申请人： AIR LIQUIDE
发明人： ALFRED ETIENNE
CPC分类号： F25J3/0233 , F25J3/0209 , F25J3/0257 , F25J3/04715 , F25J3/04872 , F25J2200/04 , F25J2200/06 , F25J2200/08 , F25J2200/10 , F25J2200/34 , F25J2200/52 , F25J2200/80 , F25J2205/02 , F25J2230/58 , F25J2250/40 , F25J2250/50 , F25J2270/06 , F25J2270/42 , F25J2290/40
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公开(公告)号：US20230235954A1
公开(公告)日：2023-07-27
申请号：US17581302
申请日：2022-01-21
发明人： Rajeev NANDA , Terence Ashley SMITHIES , Jichuan HU , Jagdish J. PIPARIA , Xun JIN , Partha GHOSAL
IPC分类号： F25J1/02
CPC分类号： F25J1/0259 , F25J1/0258 , F25J1/0283 , F25J1/0284 , F25J2210/62 , F25J2290/30 , F25J2290/60 , F25J2290/40 , F25J2290/42 , F25J2290/90
摘要： The present disclosure provides a system and method of efficiently designing a compact and modularized midscale liquefied natural gas production train. The train includes Natural Gas Pretreatment and Natural Gas Liquefaction sections designed in a unique way that reduces footprint, capital and operating cost, and overall project schedule. The train is configured into a framed compact multi-level structure with air coolers on the top level and process equipment underneath, which results in significant reduction in footprint compared to conventional stick-built design and significant reduction in footprint compared to conventional modularized design.
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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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公开(公告)号：US09823016B2
公开(公告)日：2017-11-21
申请号：US14516718
申请日：2014-10-17
申请人： Jaime A. Valencia
发明人： Jaime A. Valencia
CPC分类号： F25J3/0233 , B01D3/4211 , C07C7/05 , C10L3/101 , C10L3/104 , C10L3/106 , C10L3/107 , C10L2290/543 , C10L2290/58 , F25J1/0022 , F25J1/0027 , F25J3/0209 , F25J3/0266 , F25J3/0295 , F25J3/061 , F25J3/0635 , F25J3/08 , F25J2200/02 , F25J2200/30 , F25J2200/50 , F25J2200/74 , F25J2205/04 , F25J2205/20 , F25J2210/04 , F25J2210/80 , F25J2220/66 , F25J2235/60 , F25J2245/02 , F25J2280/10 , F25J2280/40 , F25J2290/12 , F25J2290/40 , Y02C10/12
摘要： The present disclosure provides a method for separating a feed stream in a distillation tower. The method includes operating a controlled freeze zone section in a distillation tower that separates a feed stream at a temperature and pressure at which the feed stream forms a solid in the controlled freeze zone section, wherein the feed stream includes a first contaminant; maintaining a melt tray assembly in the controlled freeze zone section; introducing the feed stream to the controlled freeze zone section; and accumulating a liquid in the melt tray assembly until the liquid is at a predetermined liquid level in the controlled freeze zone section, by: feeding a second contaminant to the controlled freeze zone section; and adding the second contaminant to the melt tray assembly, wherein the liquid comprises the second contaminant.
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公开(公告)号：US09637428B2
公开(公告)日：2017-05-02
申请号：US14462056
申请日：2014-08-18
发明人： Hank M. Hudson , John D. Wilkinson , Joe T. Lynch , Scott A. Miller , Kyle T. Cuellar , Andrew F. Johnke , W. Larry Lewis
CPC分类号： F25J3/0209 , C07C7/04 , F25J1/0022 , F25J3/0233 , F25J3/0238 , F25J3/0242 , F25J2200/02 , F25J2200/70 , F25J2200/74 , F25J2200/80 , F25J2205/04 , F25J2210/06 , F25J2215/04 , F25J2215/60 , F25J2230/20 , F25J2230/60 , F25J2235/60 , F25J2240/02 , F25J2240/40 , F25J2270/90 , F25J2290/12 , F25J2290/40 , F25J2290/80
摘要： A process and an apparatus are disclosed for a compact processing assembly to improve the recovery of C2 (or C3) and heavier hydrocarbon components from a hydrocarbon gas stream. The preferred method of separating a hydrocarbon gas stream generally includes producing at least a substantially condensed first stream and a cooled second stream, expanding both streams to lower pressure, and supplying the streams to a fractionation tower. In the process and apparatus disclosed, the expanded first stream is heated to form a vapor fraction and a liquid fraction. The vapor fraction is combined with the tower overhead vapor, directed to a heat and mass transfer means inside a processing assembly, and cooled and partially condensed by the expanded first stream to form a residual vapor stream and a condensed stream. The condensed stream is combined with the liquid fraction and supplied to the tower at its top feed point.
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公开(公告)号：US20150233645A1
公开(公告)日：2015-08-20
申请号：US14428862
申请日：2013-09-19
发明人： Jean-Pierre Tranier , Marc Wagner
IPC分类号： F28D9/00
CPC分类号： F28D9/005 , F25J3/04236 , F25J5/002 , F25J2290/32 , F25J2290/40 , F25J2290/44 , F28D9/0093
摘要： The invention relates to a heat exchanger assembly having two exchangers, each comprising a stack of parallel plates defining a first connection surface and a second connection surface that are adjacent to each other. The heat exchanger assembly can also include an enclosure between the first connection surface and the second connection surface, primary compartments in the enclosure configured to channel primary fluid through the first connection surface and the second connection surface, and a secondary compartment in the enclosure for channeling secondary fluid.
摘要翻译： 本发明涉及具有两个交换器的热交换器组件，每个交换器包括限定彼此相邻的第一连接表面和第二连接表面的平行板的堆叠。 热交换器组件还可以包括在第一连接表面和第二连接表面之间的壳体，壳体中的主隔室被配置成使主流体通过第一连接表面和第二连接表面，以及在外壳中的辅助隔室，用于引导 二次流体。
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