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公开(公告)号：US20180094772A1
公开(公告)日：2018-04-05
申请号：US15831522
申请日：2017-12-05
发明人： Pedro T. SANTOS , Scott Rackey , Jeremy Pitts , Aaron Hilber , Kolar L. Seshasai , Pedro Vergel , Jimmy Romansos
CPC分类号： F17C13/00 , F17C5/02 , F17C5/06 , F17C7/00 , F17C2201/0109 , F17C2201/035 , F17C2201/054 , F17C2205/0107 , F17C2205/0111 , F17C2205/0142 , F17C2205/0146 , F17C2205/0161 , F17C2205/0176 , F17C2205/0352 , F17C2205/0397 , F17C2221/033 , F17C2223/0123 , F17C2223/0161 , F17C2223/033 , F17C2223/035 , F17C2225/0123 , F17C2225/0161 , F17C2225/033 , F17C2225/035 , F17C2227/0346 , F17C2227/0397 , F17C2250/034 , F17C2250/036 , F17C2250/043 , F17C2250/0439 , F17C2250/0443 , F17C2250/0447 , F17C2250/0456 , F17C2250/0478 , F17C2250/0652 , F17C2265/061 , F17C2265/063 , F17C2265/065 , F17C2270/0171 , Y10T137/0318
摘要： Various embodiments provide an end-to-end gaseous fuel transportation solution without using physical pipelines. A virtual pipeline system and methods thereof may involve transportation of gaseous fuels including compressed natural gas (CNG), liquefied natural gas (LNG), and/or adsorbed natural gas (ANG). An exemplary pipeline system may include a gas supply station, a mother station for treating gaseous fuels from the gas supply station, a mobile transport system for receiving and transporting the gaseous fuels, and user site for unloading the gaseous fuels from the mobile transport system. The unloaded gaseous fuels can be further used or distributed.
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公开(公告)号：US09863581B2
公开(公告)日：2018-01-09
申请号：US14423609
申请日：2013-08-23
申请人： OSCOMP HOLDINGS INC.
发明人： Pedro T. Santos , Scott Rackey , Jeremy Pitts , Aaron Hilber , Kolar L. Seshasai , Pedro Vergel , Jimmy Romanos
CPC分类号： F17C13/00 , F17C5/02 , F17C5/06 , F17C7/00 , F17C2201/0109 , F17C2201/035 , F17C2201/054 , F17C2205/0107 , F17C2205/0111 , F17C2205/0142 , F17C2205/0146 , F17C2205/0161 , F17C2205/0176 , F17C2205/0352 , F17C2205/0397 , F17C2221/033 , F17C2223/0123 , F17C2223/0161 , F17C2223/033 , F17C2223/035 , F17C2225/0123 , F17C2225/0161 , F17C2225/033 , F17C2225/035 , F17C2227/0346 , F17C2227/0397 , F17C2250/034 , F17C2250/036 , F17C2250/043 , F17C2250/0439 , F17C2250/0443 , F17C2250/0447 , F17C2250/0456 , F17C2250/0478 , F17C2250/0652 , F17C2265/061 , F17C2265/063 , F17C2265/065 , F17C2270/0171 , Y10T137/0318
摘要： Various embodiments provide an end-to-end gaseous fuel transportation solution without using physical pipelines. A virtual pipeline system and methods thereof may involve transportation of gaseous fuels including compressed natural gas (CNG), liquefied natural gas (LNG), and/or adsorbed natural gas (ANG). An exemplary pipeline system may include a gas supply station, a mother station for treating gaseous fuels from the gas supply station, a mobile transport system for receiving and transporting the gaseous fuels, and a user site for unloading the gaseous fuels from the mobile transport system. The unloaded gaseous fuels can be further used or distributed.
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公开(公告)号：US20140245755A1
公开(公告)日：2014-09-04
申请号：US14347612
申请日：2013-05-14
发明人： Ki Hong Kim , Min Ho Kang
IPC分类号： F17C7/02
CPC分类号： F17C7/02 , C10L3/12 , F02M21/0215 , F02M21/0245 , F02M21/0284 , F02M21/06 , F17C7/04 , F17C9/00 , F17C9/02 , F17C13/025 , F17C13/026 , F17C2221/033 , F17C2221/035 , F17C2223/0153 , F17C2223/0161 , F17C2223/033 , F17C2225/035 , F17C2227/0135 , F17C2227/0302 , F17C2227/0323 , F17C2250/043 , F17C2250/0439 , F17C2250/0456 , F17C2250/0631 , F17C2250/0636 , F17C2250/0652 , F17C2250/0694 , F17C2270/0139 , F28F19/006 , F28F23/02 , F28F27/00 , Y02T10/32
摘要： Disclosed is a liquefied gas treatment system and method. A liquefied gas treatment system includes: a liquefied gas supply line connected from a liquefied gas storing tank to a source of demand, a heat exchanger provided on the liquefied gas supply line between the source of demand and the liquefied gas storing tank, and configured to heat exchange liquefied gas supplied from the liquefied gas storing tank with heat transfer media, a media heater configured to heat the heat transfer media, a media circulation line connected from the media heater to the heat exchanger, a liquefied gas temperature sensor provided on the liquefied gas supply line, and configured to measure a temperature of the liquefied gas, and a controller configured to change a flow rate of the heat transfer media flowing into the media heater or calories supplied to the heat transfer media by the media heater on the basis of the measured temperature of the liquefied gas.
摘要翻译： 公开了一种液化气处理系统和方法。 液化气处理系统包括：从液化气储存箱连接到需求源的液化气供给管线，设置在需求源与液化气储存箱之间的液化气供给管路上的热交换器， 从具有传热介质的液化气体储存罐供应的热交换液化气体，被配置为加热传热介质的介质加热器，从介质加热器连接到热交换器的介质循环管线，液化气体温度传感器 气体供给管线，并且被配置为测量液化气体的温度;以及控制器，其被配置为基于介质加热器改变流入介质加热器的传热介质的流量或由介质加热器供应到传热介质的卡路里 液化气的测量温度。
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公开(公告)号：US08056399B2
公开(公告)日：2011-11-15
申请号：US12364208
申请日：2009-02-02
IPC分类号： G01N1/00
CPC分类号： G01N1/10 , F17C6/00 , F17C9/00 , F17C13/02 , F17C2221/033 , F17C2223/0161 , F17C2223/033 , F17C2223/046 , F17C2225/0123 , F17C2225/0161 , F17C2225/033 , F17C2225/035 , F17C2227/0135 , F17C2227/0302 , F17C2227/0311 , F17C2227/0318 , F17C2227/0332 , F17C2227/0393 , F17C2250/0447 , F17C2250/0456 , F17C2260/024 , F17C2265/05 , F17C2265/061 , F17C2270/0105 , F17C2270/0136 , F17C2270/0171 , G01N1/22 , G01N33/22 , G01N33/225 , G01N2001/105 , G01N2001/2261
摘要： A liquid gas vaporization and measurement system, and associated method, for efficiently vaporizing a continuous sample of liquid gas, such as liquid natural gas (LNG), and accurately determining the constituent components of the gas. A constant flow of liquid gas sampled from a mass storage device is maintained in a vaporizing device. Within the vaporizing device the liquid gas is flash vaporized within heated narrow tubing. The liquid gas is converted to vapor very quickly as it enters one or more independently operating vaporizer stages within the vaporizing device. The vapor gas is provided to a measuring instrument such as a chromatograph and the individual constituent components and the BTU value of the gas are determined to an accuracy of within +/−0.5 mole percent and 1 BTU, respectively.
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5.发明申请公开(公告)号：US20060150640A1
公开(公告)日：2006-07-13
申请号：US11307806
申请日：2006-02-23
申请人： William Bishop
发明人： William Bishop
IPC分类号： F17C1/00
CPC分类号： F17C1/007 , F17C3/005 , F17C5/06 , F17C7/00 , F17C9/02 , F17C2201/052 , F17C2205/013 , F17C2205/0142 , F17C2205/0323 , F17C2205/0332 , F17C2205/0338 , F17C2205/0364 , F17C2221/012 , F17C2221/017 , F17C2221/033 , F17C2221/035 , F17C2223/0115 , F17C2223/0123 , F17C2223/0153 , F17C2223/0161 , F17C2223/033 , F17C2223/035 , F17C2223/036 , F17C2223/043 , F17C2223/047 , F17C2225/0115 , F17C2225/0123 , F17C2225/035 , F17C2225/036 , F17C2225/043 , F17C2225/047 , F17C2227/0135 , F17C2227/0157 , F17C2227/0164 , F17C2227/0185 , F17C2227/0192 , F17C2227/0309 , F17C2227/0316 , F17C2227/0318 , F17C2227/0323 , F17C2227/033 , F17C2227/0337 , F17C2227/0341 , F17C2227/0348 , F17C2227/0351 , F17C2227/0388 , F17C2227/039 , F17C2227/0393 , F17C2227/0395 , F17C2227/041 , F17C2227/046 , F17C2250/043 , F17C2250/0439 , F17C2250/0443 , F17C2250/0456 , F17C2250/061 , F17C2250/0626 , F17C2250/0636 , F17C2250/0657 , F17C2260/025 , F17C2265/027 , F17C2265/05 , F17C2265/068 , F17C2270/0105 , F17C2270/0121 , F17C2270/0123 , F17C2270/0136 , F17C2270/0152 , F17C2270/016 , F17C2270/0163 , F17C2270/05 , Y02E60/321 , Y10T137/0346 , Y10T137/402
摘要： In the past, “compensated” salt caverns have operated with a compensating liquid, such as brine to displace a stored liquid, such as crude oil, when the stored liquid is needed on the surface. Virtually all of the stored liquid in a compensated salt cavern can be expelled from the salt cavern when it is filled with the compensating liquid. In the past, “uncompensated” salt caverns have been used to store gases, such as natural gas. Uncompensated caverns operate without any compensating liquid; instead they rely on pressure. Some of the stored gas (cushion gas) must always be left in an uncompensated salt cavern. This invention breaks with convention and uses a compensating liquid in a salt cavern to store gases which is a technique believed to be previously unknown. “Cushion gas” is not required because the compensating liquid displaces virtually all of the gas in the salt cavern.
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公开(公告)号：US4302943A
公开(公告)日：1981-12-01
申请号：US201947
申请日：1980-10-29
IPC分类号： F17C13/02
CPC分类号： F17C13/026 , F17C2203/0629 , F17C2205/0358 , F17C2221/014 , F17C2221/017 , F17C2223/0161 , F17C2223/033 , F17C2227/0304 , F17C2227/0374 , F17C2250/0408 , F17C2250/0439 , F17C2250/0443 , F17C2250/0456 , F17C2250/0495 , F17C2270/0509 , Y10T137/7306
摘要： A method is provided for measuring the heat influx of a cryogenic transfer system. A gaseous phase of the cryogen used during normal operation of the system is passed through the system. The gaseous cryogen at the inlet to the system is tempered to duplicate the normal operating temperature of the system inlet. The temperature and mass flow rate of the gaseous cryogen is measured at the outlet of the system, and the heat capacity of the cryogen is determined. The heat influx of the system is then determined from known thermodynamic relationships.
摘要翻译： 提供了一种用于测量低温转移系统的热量的方法。 在系统的正常操作期间使用的制冷剂的气相通过系统。 在系统入口处的气态冷冻剂被回火以复制系统入口的正常工作温度。 在系统的出口处测量气态冷冻剂的温度和质量流量，并确定冷冻剂的热容量。 然后从已知的热力学关系确定系统的热量。
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公开(公告)号：US20140150470A1
公开(公告)日：2014-06-05
申请号：US14131675
申请日：2013-05-14
发明人： Ju Seog Han , Eun Sung Baek
IPC分类号： C10L3/12
CPC分类号： F17C7/02 , C10L3/12 , F02M21/0215 , F02M21/0245 , F02M21/0284 , F02M21/06 , F17C7/04 , F17C9/00 , F17C9/02 , F17C13/025 , F17C13/026 , F17C2221/033 , F17C2221/035 , F17C2223/0153 , F17C2223/0161 , F17C2223/033 , F17C2225/035 , F17C2227/0135 , F17C2227/0302 , F17C2227/0323 , F17C2250/043 , F17C2250/0439 , F17C2250/0456 , F17C2250/0631 , F17C2250/0636 , F17C2250/0652 , F17C2250/0694 , F17C2270/0139 , F28F19/006 , F28F23/02 , F28F27/00 , Y02T10/32
摘要： Disclosed is a liquefied gas processing system and method. A liquefied gas treatment system includes: a liquefied gas supply line connected from a liquefied gas storing tank to a source of demand, a pump provided on the liquefied gas supply line, and configured to pressurize liquefied gas discharged from the liquefied gas storing tank, a heat exchanger provided on the liquefied gas supply line between the source of demand and the pump, and configured to heat exchange the liquefied gas supplied from the pump with heat transfer media, a media heater configured to heat the heat transfer media, a media circulation line connected from the media heater to the heat exchanger, and a controller configured to change a flow rate of the heat transfer media flowing into the media heater or calories supplied to the heat transfer media by the media heater on the basis of a flow rate of the liquefied gas supplied to the heat exchanger.
摘要翻译： 公开了一种液化气处理系统和方法。 液化气处理系统包括：液化气供给管线，其从液化气储存罐连接到需求源，设置在液化气供给管路上的泵，构成为对从液化气储存罐排出的液化气体进行加压， 设置在需求源与泵之间的液化气供应管线上的热交换器，并且构造成用热传递介质热泵交换从泵供应的液化气体，配置成加热传热介质的介质加热器，介质循环管线 从介质加热器连接到热交换器，以及控制器，其被配置为基于介质加热器的流量来改变流入介质加热器的传热介质的流量或由介质加热器供应到传热介质的卡路里 供应到热交换器的液化气。
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8.发明申请LNG RECEIVING TERMINAL THAT PRIMARILY USES COMPENSATED SALT CAVERN STORAGE AND METHOD OF USE 审中-公开液化天然气接收终端，主要使用补偿性盐储存和使用方法公开(公告)号：US20090010714A1
公开(公告)日：2009-01-08
申请号：US12209385
申请日：2008-09-12
申请人： William M. Bishop
发明人： William M. Bishop
CPC分类号： F17C1/007 , F17C3/005 , F17C5/06 , F17C7/00 , F17C9/02 , F17C2201/052 , F17C2205/013 , F17C2205/0142 , F17C2205/0323 , F17C2205/0332 , F17C2205/0338 , F17C2205/0364 , F17C2221/012 , F17C2221/017 , F17C2221/033 , F17C2221/035 , F17C2223/0115 , F17C2223/0123 , F17C2223/0153 , F17C2223/0161 , F17C2223/033 , F17C2223/035 , F17C2223/036 , F17C2223/043 , F17C2223/047 , F17C2225/0115 , F17C2225/0123 , F17C2225/035 , F17C2225/036 , F17C2225/043 , F17C2225/047 , F17C2227/0135 , F17C2227/0157 , F17C2227/0164 , F17C2227/0185 , F17C2227/0192 , F17C2227/0309 , F17C2227/0316 , F17C2227/0318 , F17C2227/0323 , F17C2227/033 , F17C2227/0337 , F17C2227/0341 , F17C2227/0348 , F17C2227/0351 , F17C2227/0388 , F17C2227/039 , F17C2227/0393 , F17C2227/0395 , F17C2227/041 , F17C2227/046 , F17C2250/043 , F17C2250/0439 , F17C2250/0443 , F17C2250/0456 , F17C2250/061 , F17C2250/0626 , F17C2250/0636 , F17C2250/0657 , F17C2260/025 , F17C2265/027 , F17C2265/05 , F17C2265/068 , F17C2270/0105 , F17C2270/0121 , F17C2270/0123 , F17C2270/0136 , F17C2270/0152 , F17C2270/016 , F17C2270/0163 , F17C2270/05 , Y02E60/321 , Y10T137/0346 , Y10T137/402
摘要： In the past, “compensated” salt caverns have operated with a compensating liquid, such as brine to displace a stored liquid, such as crude oil, when the stored liquid is needed on the surface. Virtually all of the stored liquid in a compensated salt cavern can be expelled from the salt cavern when it is filled with the compensating liquid. In the past, “uncompensated” salt caverns have been used to store gases, such as natural gas. Uncompensated caverns operate without any compensating liquid; instead they rely on pressure. Some of the stored gas (cushion gas) must always be left in an uncompensated salt cavern. This invention breaks with convention and uses a compensating liquid in a salt cavern to store gases which is a technique believed to be previously unknown. “Cushion gas” is not required because the compensating liquid displaces virtually all of the gas in the salt cavern.
摘要翻译： 过去，当需要储存的液体在表面上时，“补偿”的盐穴用补偿液体（例如盐水）操作以置换诸如原油的储存液体。 实际上，补偿盐穴中的所有储存液体当填充补偿液体时都可以从盐穴中排出。 过去，“未补偿”的盐穴已被用于储存气体，如天然气。 未补偿的洞穴无补偿液体; 而是依靠压力。 一些储存气体（缓冲气体）必须始终留在未补偿的盐穴中。 本发明符合惯例，并且在盐穴中使用补偿液体来储存气体，这是以前未知的技术。 不需要“缓冲气体”，因为补偿液体几乎全部置换了盐穴中的所有气体。
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9.发明申请公开(公告)号：US20080295527A1
公开(公告)日：2008-12-04
申请号：US11971103
申请日：2008-01-08
申请人： Jung Han Lee , Jong Hyun Park , Young Soo Kim , Hyun Ki Park , Jin Yul Yu , Hyun Jin Kim
发明人： Jung Han Lee , Jong Hyun Park , Young Soo Kim , Hyun Ki Park , Jin Yul Yu , Hyun Jin Kim
IPC分类号： F17C9/02
CPC分类号： F25J3/044 , F17C5/06 , F17C9/02 , F17C2205/0341 , F17C2221/014 , F17C2221/033 , F17C2223/0153 , F17C2223/0161 , F17C2223/033 , F17C2225/0123 , F17C2225/035 , F17C2227/0135 , F17C2227/0178 , F17C2227/0393 , F17C2250/0456 , F17C2250/0652 , F17C2265/025 , F17C2265/05 , F17C2270/0105 , F17C2270/0123 , F17C2270/0136 , F25J3/04266 , F25J3/04563 , F25J3/04987 , F25J2200/74
摘要： Disclosed is an apparatus for producing nitrogen equipped in a marine structure such as a liquefied natural gas regasification vessel (LNG RV) and a floating storage and regasification unit (FSRU), and a method for producing nitrogen in a marine structure using the apparatus. The apparatus for producing nitrogen equipped in a flowing marine structure produces nitrogen to be mixed with natural gas to be supplied to consumers after regasification. The floating marine structure in which the apparatus is equipped has an LNG regasification facility for compressing the LNG stored in a storage tank using a high-pressure pump and then vaporizing the LNG into natural gas in a vaporizer to supply natural gas to consumers. The apparatus for producing nitrogen secures cold heat necessary to produce nitrogen using the LNG supplied from the storage tank.
摘要翻译： 公开了一种用于生产装备在诸如液化天然气再气化容器（LNG RV）和浮选储存和再气化单元（FSRU）的海洋结构中的氮的装置，以及使用该装置在海洋结构中产生氮的方法。 用于生产装备在流动海洋结构中的氮的装置在再气化后产生氮气以与天然气混合供应给消费者。 配备有该装置的浮动海洋结构具有用于使用高压泵压缩储存在储罐中的LNG的LNG再气化设备，然后将LNG蒸发成蒸发器中的天然气，以向消费者提供天然气。 用于生产氮气的设备使用从储罐供应的LNG确保产生氮气所需的冷热。
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公开(公告)号：US20050155357A1
公开(公告)日：2005-07-21
申请号：US10907330
申请日：2005-03-29
申请人： William Bishop , Michael McCall
发明人： William Bishop , Michael McCall
CPC分类号： F17C3/005 , F17C5/06 , F17C7/00 , F17C9/02 , F17C2205/0364 , F17C2221/033 , F17C2223/0115 , F17C2223/0123 , F17C2223/0161 , F17C2223/033 , F17C2225/0115 , F17C2225/0123 , F17C2225/035 , F17C2225/036 , F17C2227/0135 , F17C2227/0157 , F17C2227/0185 , F17C2227/0309 , F17C2227/0316 , F17C2227/0318 , F17C2227/0323 , F17C2227/033 , F17C2227/0337 , F17C2227/0388 , F17C2227/0393 , F17C2227/0395 , F17C2250/0456 , F17C2265/05 , F17C2265/068 , F17C2270/0105 , F17C2270/0152
摘要： The Dual Gas Facility stores natural gas in one or more man-made salt caverns typically located in a single salt dome or in bedded salt. The Dual Gas Facility can access different sources of natural gas. A first gas source is from a natural gas pipeline(s) and a second gas source is from LNG. Depending on economic conditions, supply conditions and other factors, the Dual Gas Facility can receive gas from the natural gas pipeline(s) and/or from LNG to fill the salt caverns. Of course, the LNG must be warmed before being stored in a salt cavern.
摘要翻译： 双重气体设施将天然气储存在一个或多个人造盐穴中，通常位于单个盐穹顶或床层盐中。 双气体设施可以访问不同的天然气来源。 第一气源来自天然气管道，第二气源来自LNG。 根据经济状况，供应条件和其他因素，双燃气设施可以从天然气管道和/或LNG接收天然气以填充盐洞。 当然，LNG必须在储存在盐穴中之前加热。
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