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41.发明授权公开(公告)号：US09815751B2
公开(公告)日：2017-11-14
申请号：US13993211
申请日：2011-12-20
CPC分类号： C07C5/05 , C07C2/84 , C10G3/00 , C10G9/00 , C10G45/32 , C10G57/00 , C10G69/06 , C10G70/02 , Y02P30/20
摘要： The invention relates to hydrocarbon conversion processes, e.g., to processes for producing acetylene from hydrocarbon and then hydrogenating at least a portion of the acetylene. The invention also relates to polymerizing one or more products derived from the acetylene saturation, and to equipment useful for these processes.
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42.发明授权公开(公告)号：US09708231B2
公开(公告)日：2017-07-18
申请号：US13994476
申请日：2011-12-20
IPC分类号： C07C4/04 , C10G47/02 , C07C5/09 , B01J19/24 , C08F110/02
CPC分类号： C07C4/04 , B01J19/245 , B01J2219/24 , C07C5/09 , C08F110/02 , C10G47/02 , C07C11/04 , C07C11/24
摘要： An apparatus and method are provided for processing hydrocarbon feeds. The method may contact hydrogen (H2) and a hydrocarbon feed containing ≧10 wt % resid in the hydrocarbon feed with a catalyst to form a hydroprocessed product. Then, a pyrolysis feed derived from the hydroprocessed product is exposed at high-severity thermal pyrolysis operating conditions to produce a reactor product that comprises ethylene and acetylene. Further, at least a portion of the hydrogen (H2) may be separated from the reactor product, wherein the hydrogen (H2) contacting the catalyst includes at least a portion of the separated hydrogen (H2).
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公开(公告)号：US09677014B2
公开(公告)日：2017-06-13
申请号：US13994229
申请日：2011-12-20
IPC分类号： B01D3/00 , C07C5/09 , C08F10/06 , C08F10/02 , B01J19/24 , C10G55/04 , C07C2/76 , C10G9/00 , C10G9/16 , C10G9/18 , C10G9/26
CPC分类号： C10G55/04 , B01D3/009 , B01J19/245 , B01J2219/24 , C07C2/76 , C08F10/02 , C08F10/06 , C10G9/002 , C10G9/005 , C10G9/007 , C10G9/16 , C10G9/18 , C10G9/26 , C07C11/24 , C07C11/04 , C07C11/06
摘要： An apparatus and process are provided for processing hydrocarbon feeds. The process enhances the conversion of hydrocarbon feeds into conversion products, such as ethylene and propylene. In particular, the present techniques utilize two high-severity pyrolysis reactors integrated with another reactor type to convert hydrocarbons to other petrochemical products. The pyrolysis reactors recycle a portion of one of the reactor products to at least one of the pyrolysis reactors to further enhance the process.
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44.发明授权公开(公告)号：US09676681B2
公开(公告)日：2017-06-13
申请号：US13994461
申请日：2011-12-20
IPC分类号： C07C4/04
摘要： An apparatus and method are provided for processing hydrocarbon feeds. The method enhances the conversion of hydrocarbon feeds into conversion products, such as ethylene and propylene. In particular, the present techniques combine a first hydrocarbon feed with a second hydrocarbon feed and a hydrogen (H2) containing stream to manage the hydrogen content of the feed provided to a pyrolysis reactor. The mixture is then exposed to high-severity operating conditions in a pyrolysis reactor and further processing into desired olefins.
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45.发明授权公开(公告)号：US09505680B2
公开(公告)日：2016-11-29
申请号：US13994491
申请日：2011-12-20
摘要： An apparatus and method are provided for processing hydrocarbon feeds. The method enhances the conversion of hydrocarbon feeds into ethylene. In particular, the present techniques expose feed containing hydrocarbons to high-severity operating conditions in a pyrolysis reactor and separate the reactor product from the reactor into a first product having hydrogen and a second product including ≧90 mole percent of the acetylene in the reactor product. Then, the second product is reacted with a catalyst in a converter to form ethylene.
摘要翻译： 提供了一种用于处理烃进料的装置和方法。 该方法增强了碳氢化合物进料转化为乙烯。 特别地，本技术将含碳氢化合物的原料暴露于热解反应器中的高苛刻度操作条件下，并将反应器产物与反应器分离成具有氢气的第一产物和包含反应器产物中的≥90摩尔％乙炔的第二产物 。 然后，将第二产物与转化器中的催化剂反应以形成乙烯。
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公开(公告)号：US20140303418A1
公开(公告)日：2014-10-09
申请号：US13994433
申请日：2011-12-20
CPC分类号： C07C2/78 , C07C2/06 , C07C4/06 , C07C5/09 , C07C7/00 , C07C7/14858 , C07C2521/04 , C07C2521/08 , C07C2521/12 , C07C2523/42 , C07C2523/44 , C07C2523/50 , C10G50/00 , C10G2300/1025 , C10G2300/202 , C10G2300/207 , C10G2400/20 , C10G2400/22 , C10G2400/24 , Y02P30/40 , C07C11/24 , C07C11/04
摘要： The invention relates to processes for converting a mixture of hydrocarbon and sulfur-containing molecules such as mercaptan into products comprising acetylene, ethylene, and hydrogen sulfide, to processes utilizing the acetylene and ethylene resulting from the conversion, and to equipment useful for such processes.
摘要翻译： 本发明涉及将烃和含硫分子如硫醇的混合物转化成包含乙炔，乙烯和硫化氢的产物的方法，以利用由转化产生的乙炔和乙烯的方法，以及可用于这些方法的设备。
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公开(公告)号：US20140303339A1
公开(公告)日：2014-10-09
申请号：US13993522
申请日：2011-12-20
IPC分类号： C07C4/04 , C08F110/02 , C08F110/06 , C07C5/09
CPC分类号： C07C4/04 , C07C2/76 , C08F110/02 , C08F110/06 , C10G9/00 , C10G9/002 , C10G9/007 , C10G9/16 , C10G9/18 , C10G9/26 , C10G9/38 , C07C11/24 , C07C11/04
摘要： An apparatus and method are provided for processing hydrocarbon feeds. The method enhances the conversion of hydrocarbon feeds into conversion products, such as ethylene and propylene. In particular, the present techniques utilize a high-severity reactor integrated with another reactor type to convert hydrocarbons to other petrochemical products.
摘要翻译： 提供了一种用于处理烃进料的装置和方法。 该方法增强了烃进料转化成转化产物，如乙烯和丙烯。 特别地，本技术利用与另一反应器类型相结合的高等级反应器将碳氢化合物转化为其它石化产品。
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公开(公告)号：US20130211169A1
公开(公告)日：2013-08-15
申请号：US13588821
申请日：2012-08-17
申请人： Frank Hershkowitz , Paul F. Keusenkothen , Jeffrey W. Frederick , Richard J. Basile , John W. Fulton
发明人： Frank Hershkowitz , Paul F. Keusenkothen , Jeffrey W. Frederick , Richard J. Basile , John W. Fulton
CPC分类号： C10G9/16 , B01J19/2485 , B01J2219/00164 , B01J2219/2411 , B01J2219/2419 , B01J2219/2434 , C07C5/327 , C07C5/333 , C07C5/35 , C10B23/00 , C10B27/06 , C10B43/10 , C10B47/02 , C10G9/18 , C10G9/26 , C10G2400/20
摘要： The invention relates to a process for converting hydrocarbons into unsaturated products such as acetylene and/or ethylene. The invention also relates to converting acetylene to olefins such as ethylene and/or propylene, to polymerizing the olefins, and to equipment useful for these processes.
摘要翻译： 本发明涉及将烃转化为不饱和产物如乙炔和/或乙烯的方法。 本发明还涉及将乙炔转化为烯烃如乙烯和/或丙烯以使烯烃聚合，以及可用于这些方法的设备。
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公开(公告)号：US20100288617A1
公开(公告)日：2010-11-18
申请号：US12576002
申请日：2009-10-08
IPC分类号： C10B57/16 , C04B35/01 , B01J8/00 , B01J19/00 , C10B23/00 , C10G9/00 , C10B47/00 , C10B1/00 , C07C4/04 , C07C4/06
CPC分类号： C04B35/488 , B01J4/002 , B01J8/0438 , B01J8/0442 , B01J8/0492 , B01J19/02 , B01J19/2485 , B01J2208/00115 , B01J2208/00309 , B01J2208/00504 , B01J2208/0084 , B01J2208/00849 , B01J2219/00081 , B01J2219/00117 , B01J2219/00157 , B01J2219/00159 , B01J2219/0263 , C04B35/486 , C04B35/505 , C04B2235/3206 , C04B2235/3208 , C04B2235/3217 , C04B2235/3224 , C04B2235/3225 , C04B2235/3227 , C04B2235/3229 , C04B2235/3232 , C04B2235/3239 , C04B2235/3241 , C04B2235/3244 , C04B2235/3246 , C04B2235/3251 , C04B2235/3256 , C04B2235/3258 , C04B2235/3262 , C04B2235/3272 , C04B2235/3275 , C04B2235/3279 , C04B2235/3418 , C04B2235/528 , C04B2235/5296 , C04B2235/5436 , C04B2235/5445 , C04B2235/5472 , C04B2235/5481 , C04B2235/6021 , C04B2235/658 , C04B2235/6584 , C04B2235/72 , C04B2235/762 , C04B2235/77 , C04B2235/96 , C04B2235/9607 , C04B2235/9669 , C04B2235/9684 , C10G1/02 , C10G9/00 , C10G9/005 , C10G9/18 , C10G9/26 , C10G75/00 , Y02P20/582
摘要： In one aspect, the invention includes a reactor apparatus for pyrolyzing a hydrocarbon feedstock, the apparatus including: a reactor component comprising a refractory material in oxide form, the refractory material having a melting point of at least 2060° C. and which remains in oxide form when exposed to a gas having carbon partial pressure of 10−22 bar, an oxygen partial pressure of 10−10 bar, at a temperature of 1200° C. In some embodiments, the reactor comprises a regenerative pyrolysis reactor apparatus and in other embodiments it includes a reverse flow regenerative reactor apparatus. In other aspects, this invention includes a method for pyrolyzing a hydrocarbon feedstock using a pyrolysis reactor system comprising the step of providing in a heated region of a pyrolysis reactor system for pyrolyzing a hydrocarbon feedstock, apparatus comprising a refractory material in oxide form, the refractory material having a melting point of at least 2060° C. and that remains in oxide form when exposed to a gas having a carbon partial pressure of 10−22 bar, an oxygen partial pressure of 10−10 bar, at a temperature of 1200° C.
摘要翻译： 在一个方面，本发明包括用于热解烃原料的反应器装置，该装置包括：反应器组件，其包含氧化物形式的耐火材料，耐火材料的熔点至少为2060℃，并保留在氧化物 当暴露于碳分压为10-22巴，氧气分压为10-10巴的气体时，在1200℃的温度下形成。在一些实施方案中，反应器包括再生热解反应器装置，在其它实施方案中 它包括逆流再生反应器装置。 在其他方面，本发明包括使用热解反应器系统热解烃原料的方法，该方法包括在加热区域中提供用于热解烃原料的热解反应器系统，包括氧化物形式的耐火材料的装置，耐火材料 材料具有至少2060℃的熔点，并且当暴露于碳分压为10-22巴，氧分压为10-10巴的气体时，在1200℃的温度下保持为氧化物形式 C。
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公开(公告)号：US09819042B2
公开(公告)日：2017-11-14
申请号：US14325664
申请日：2014-07-08
IPC分类号： H01M8/14 , H01M8/04 , H01M8/24 , H01M8/04007 , H01M8/249 , C01B3/50 , C10K3/04 , C10G2/00 , H01M8/0668 , H01M8/2475 , F01K5/02
CPC分类号： H01M8/145 , C01B3/50 , C01B2203/0233 , C01B2203/0283 , C01B2203/0405 , C01B2203/0415 , C01B2203/043 , C01B2203/046 , C01B2203/0475 , C01B2203/0495 , C01B2203/061 , C01B2203/062 , C01B2203/066 , C01B2203/067 , C01B2203/148 , C01B2203/84 , C01B2203/86 , C10G2/32 , C10G2300/4043 , C10K3/04 , F01K5/02 , H01M8/04007 , H01M8/04067 , H01M8/0668 , H01M8/2475 , H01M8/249 , H01M2008/147 , H01M2250/405 , Y02B90/16 , Y02E20/16 , Y02E60/526 , Y02E60/566 , Y02P20/129 , Y02P20/13 , Y02P30/30 , Y02P30/446
摘要： Systems and methods are provided for incorporating molten carbonate fuel cells into a heat recovery steam generation system (HRSG) for production of electrical power while also reducing or minimizing the amount of CO2 present in the flue gas exiting the HRSG. An optionally multi-layer screen or wall of molten carbonate fuel cells can be inserted into the HRSG so that the screen of molten carbonate fuel cells substantially fills the cross-sectional area. By using the walls of the HRSG and the screen of molten carbonate fuel cells to form a cathode input manifold, the overall amount of duct or flow passages associated with the MCFCs can be reduced.
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