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公开(公告)号：US20070125122A1
公开(公告)日：2007-06-07
申请号：US10578122
申请日：2004-06-17
Applicant: John Mak , Richard Nielsen , Curt Graham
Inventor： John Mak , Richard Nielsen , Curt Graham
CPC classification number: F17C9/00 , F17C3/00 , F17C5/06 , F17C6/00 , F17C9/04 , F17C2201/052 , F17C2205/0364 , F17C2205/0367 , F17C2221/033 , F17C2221/035 , F17C2223/0161 , F17C2223/033 , F17C2223/043 , F17C2223/047 , F17C2225/0123 , F17C2225/0153 , F17C2225/0161 , F17C2225/033 , F17C2225/035 , F17C2225/036 , F17C2225/047 , F17C2227/0128 , F17C2227/0135 , F17C2227/0157 , F17C2227/0178 , F17C2227/0185 , F17C2227/0306 , F17C2227/0309 , F17C2227/0318 , F17C2227/0327 , F17C2227/0339 , F17C2227/0388 , F17C2227/0393 , F17C2250/0636 , F17C2250/0642 , F17C2260/02 , F17C2260/031 , F17C2260/056 , F17C2265/015 , F17C2265/022 , F17C2265/025 , F17C2265/03 , F17C2265/033 , F17C2265/034 , F17C2265/036 , F17C2265/037 , F17C2265/05 , F17C2270/0105 , F17C2270/0123 , F17C2270/0136 , F25J3/0214 , F25J3/0233 , F25J3/0242 , F25J2200/02 , F25J2205/90 , F25J2210/04 , F25J2210/62 , F25J2210/90 , F25J2235/60 , F25J2245/02 , F25J2245/90 , F25J2270/904 , F25J2290/62
Abstract: LNG vapor from an LNG storage vessel is absorbed using C3 and heavier components provided by a fractionator that receives a mixture of LNG vapors and the C3 and heavier components as fractionator feed. In such configurations, refrigeration content of the LNG liquid from the LNG storage vessel is advantageously used to condense the LNG vapor after separation. Where desired, a portion of the LNG liquid may also be used as fractionator feed to produce LPG as a bottom product.
Abstract translation: 来自LNG储存容器的LNG蒸汽被C 3 3和较重的组分吸收，分馏塔由接收LNG蒸汽和C 3 3重质组分的混合物的分馏器提供，作为分馏塔进料 。 在这种构造中，来自LNG储存容器的LNG液体的制冷含量有利地用于在分离后冷凝LNG蒸气。 在需要的情况下，一部分LNG液体也可以用作分馏器进料以产生作为底部产物的LPG。
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公开(公告)号：US07192468B2
公开(公告)日：2007-03-20
申请号：US10478350
申请日：2002-04-15
Applicant: John Mak , Curt Graham , Richard Nielsen
Inventor： John Mak , Curt Graham , Richard Nielsen
IPC: B01D53/14
CPC classification number: C10L3/102 , B01D53/1475 , C10L3/10 , Y02C10/06
Abstract: A plant includes an absorber (103) that operates in a gas phase supercritical region and removes an acid gas from a feed stream (9) at high recovery of the feed stream (10) while producing a high purity acid gas stream (36). Particularly preferred plants include gas purification plants that receive a feed gas with at least 5 mol % carbon dioxide at a pressure of at least 3000 psi.
Abstract translation: 植物包括在气相超临界区域中操作并在高回收率的进料流（10）中从进料流（9）中除去酸性气体同时产生高纯酸性气流（36）的吸收器（103）。 特别优选的设备包括气体净化设备，其在至少3000psi的压力下接收具有至少5mol％二氧化碳的进料气体。
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公开(公告)号：US20050000360A1
公开(公告)日：2005-01-06
申请号：US10478350
申请日：2002-04-15
Applicant: John Mak , Curt Graham , Richard Nielsen
Inventor： John Mak , Curt Graham , Richard Nielsen
CPC classification number: C10L3/102 , B01D53/1475 , C10L3/10 , Y02C10/06
Abstract: A plant includes an absorber (103) that operates in a gas phase supercritical region and removes an acid gas from a feed stream (9) at high recovery of the feed stream (10) while producing a high purity acid gas stream (36). Particularly preferred plants include gas purification plants that receive a feed gas with at least 5 mol % carbon dioxide at a pressure of at least 3000 psi.
Abstract translation: 植物包括在气相超临界区域中操作并在高回收率的进料流（10）中从进料流（9）中除去酸性气体同时产生高纯酸性气流（36）的吸收器（103）。 特别优选的设备包括气体净化设备，其在至少3000psi的压力下接收具有至少5mol％二氧化碳的进料气体。
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Patent Agency Ranking
4.发明申请Configurations And Methods For Carbon Dioxide And Hydrogen Production From Gasification Streams 有权二氧化碳的配置和方法以及气化炉的氢气生产公开(公告)号：US20100111784A1
公开(公告)日：2010-05-06
申请号：US12526617
申请日：2008-02-22
Applicant: John Mak , Richard Nielsen
Inventor： John Mak , Richard Nielsen
CPC classification number: B01D53/1462 , B01D53/1406 , B01D53/1475 , B01D2256/16 , B01D2257/304 , B01D2257/504 , C01B3/52 , C01B17/04 , C01B17/0456 , C01B17/164 , C01B32/50 , C01B2203/0415 , C01B2203/0475 , C01B2203/0485 , C01B2203/86 , Y02C10/04 , Y02C10/06 , Y02P20/152 , Y02P30/30
Abstract: A syngas treatment plant is configured to remove sulfurous compounds and carbon dioxide from shifted or un-shifted syngas in a configuration having a decarbonization section and a desulfurization section. Most preferably, the solvent in the decarbonization section is regenerated and cooled by flashing, while the solvent is regenerated in the desulfurization section via stripping using external heat, and it is still further preferred that carbonylsulfide is removed in the desulfurization section via hydrolysis, and that the so produced hydrogen sulfide is removed in a downstream absorber.
Abstract translation: 合成气处理装置被配置为在具有脱碳部分和脱硫部分的构造中从移位或未位移的合成气中除去亚硫酸化合物和二氧化碳。 最优选的是，脱碳部分中的溶剂通过闪蒸再生和冷却，而在脱硫部分中通过外部热量汽提再生溶剂，并且还优选通过水解在脱硫部分除去羰硫醚，并且 在下游的吸收塔中除去所生成的硫化氢。
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公开(公告)号：US20050211092A1
公开(公告)日：2005-09-29
申请号：US10478390
申请日：2002-11-25
Applicant: Richard Nielsen , John Mak
Inventor： Richard Nielsen , John Mak
CPC classification number: B01D53/40 , B01D53/1456
Abstract: Contemplated plants comprise an acid gas removal unit (102) that receives a compressed gas from an injection gas compressor (107), wherein acid gas is removed from the compressed gas in the acid gas removal unit (102) at a pressure of about of above pipeline pressure.
Abstract translation: 考虑的设备包括从喷射气体压缩机（107）接收压缩气体的酸性气体去除单元（102），其中在大约上述压力下从酸性气体去除单元（102）中的压缩气体中除去酸性气体 管道压力。
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6.发明授权公开(公告)号：US08480982B2
公开(公告)日：2013-07-09
申请号：US12526617
申请日：2008-02-22
Applicant: John Mak , Richard Nielsen
Inventor： John Mak , Richard Nielsen
CPC classification number: B01D53/1462 , B01D53/1406 , B01D53/1475 , B01D2256/16 , B01D2257/304 , B01D2257/504 , C01B3/52 , C01B17/04 , C01B17/0456 , C01B17/164 , C01B32/50 , C01B2203/0415 , C01B2203/0475 , C01B2203/0485 , C01B2203/86 , Y02C10/04 , Y02C10/06 , Y02P20/152 , Y02P30/30
Abstract: A syngas treatment plant is configured to remove sulfurous compounds and carbon dioxide from shifted or un-shifted syngas in a configuration having a decarbonization section and a desulfurization section. Most preferably, the solvent in the decarbonization section is regenerated and cooled by flashing, while the solvent is regenerated in the desulfurization section via stripping using external heat, and it is still further preferred that carbonylsulfide is removed in the desulfurization section via hydrolysis, and that the so produced hydrogen sulfide is removed in a downstream absorber.
Abstract translation: 合成气处理装置被配置为在具有脱碳部分和脱硫部分的构造中从移位或未位移的合成气中除去亚硫酸化合物和二氧化碳。 最优选的是，脱碳部分中的溶剂通过闪蒸再生和冷却，而在脱硫部分中通过外部热量汽提再生溶剂，并且还优选通过水解在脱硫部分除去羰硫醚，并且 在下游的吸收塔中除去所生成的硫化氢。
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公开(公告)号：US20070267353A1
公开(公告)日：2007-11-22
申请号：US10595527
申请日：2004-11-12
Applicant: John Mak , Richard Nielsen
Inventor： John Mak , Richard Nielsen
IPC: C02F1/00
Abstract: A filter system has a first filter from which solvent is recovered in a cleaning cycle using a rinse fluid in forward flow, and from which particulates are removed using flush gas in reverse flow. At least part of the solvent and the flush gas are recycled to the system and in still further preferred aspects, filtration of the solvent continues during the cleaning cycle via a bypass circuit through which the solvent is routed to a second filter.
Abstract translation: 过滤器系统具有第一过滤器，在清洁循环中使用前向冲洗流体回收溶剂，并且使用逆流中的冲洗气体从其中除去微粒。 溶剂和冲洗气体的至少一部分被再循环到系统中，并且在另外优选的方面，溶剂的过滤在清洁循环期间经由旁路回路，溶剂通过旁路回路路由到第二过滤器。
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8.发明申请Device and method for on-orbit calibration verification of an infrared sensor 有权一种用于红外传感器轨道校准验证的装置和方法公开(公告)号：US20050051670A1
公开(公告)日：2005-03-10
申请号：US10654454
申请日：2003-09-04
Applicant: David Geyer , Russell Ferring , Richard Nielsen
Inventor： David Geyer , Russell Ferring , Richard Nielsen
CPC classification number: B64G1/36 , B64G1/66 , G01J5/522 , G01N21/274
Abstract: A device for verifying the calibration of an infrared sensor includes a body configured to be placed in orbit. The body defines a spin axis and an outer surface. The outer surface has an infrared radiant intensity that is substantially independent of the viewing angle between the spin axis of the body and the infrared sensor. The device may be used for on-orbit verification of the calibration coefficients associated with each pixel of an infrared sensor, including linearity calibration and verification of the resolution capability of the sensor. The calibration coefficients may be verified over the entire sensing capability range of the infrared sensor. After a thermal model of the device is developed, the device operates passively and provides a known source of infrared radiation observable during the device's entire orbital lifetime. The device may be designed to automatically de-orbit from space after a predictable time in orbit.
Abstract translation: 用于验证红外传感器的校准的装置包括配置成放置在轨道上的主体。 主体定义了旋转轴和外表面。 外表面具有基本上与身体的旋转轴与红外线传感器之间的视角无关的红外辐射强度。 该装置可以用于对与红外线传感器的每个像素相关联的校准系数进行在轨验证，包括线性校准和传感器的分辨能力的验证。 可以在红外传感器的整个感测能力范围内验证校准系数。 在开发了器件的热模型之后，器件被动地进行操作，并在器件的整个轨道寿命期间提供可见的红外辐射源。 该设备可以被设计成在轨道上的可预测时间之后自动地从太空中行走。
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