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1.发明申请公开(公告)号：US20080081938A1
公开(公告)日：2008-04-03
申请号：US11541200
申请日：2006-09-28
IPC分类号： C07C4/02
CPC分类号： C07C7/005 , B01D53/1475 , B01D53/77 , B01D2256/24 , B01D2257/504 , C07C7/11 , C10G9/206 , C10G2400/20 , Y02C10/06 , Y02P20/152 , Y02P20/51 , Y02P20/52 , Y02P30/40 , Y02P30/442 , C07C11/06 , C07C11/04
摘要： Processing schemes and arrangements for the amine treatment of high olefin content (e.g., ethylene-rich) carbon dioxide-containing streams such as for the effective separation and removal of carbon dioxide therefrom are provided. Corresponding or associated processing schemes and arrangements for the catalytic cracking of a heavy hydrocarbon feedstock and obtaining light olefins substantially free of carbon dioxide via absorption-based product recovery are also provided.
摘要翻译： 提供了用于胺处理高烯烃含量（例如富含乙烯的二氧化碳）流的方法和装置，以便有效分离和除去二氧化碳。 还提供了通过基于吸收的产物回收的重烃原料的催化裂化和获得基本上不含二氧化碳的轻质烯烃的相应或相关的处理方案和装置。
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2.发明授权公开(公告)号：US08007661B1
公开(公告)日：2011-08-30
申请号：US11643884
申请日：2006-12-21
IPC分类号： C10G11/18
CPC分类号： C10G11/18
摘要： Processing schemes and arrangements are provided arrangements are provided for the processing a heavy hydrocarbon feedstock via hydrocarbon cracking processing with selected hydrocarbon fractions being obtained via absorption-based product recovery while minimizing or avoiding loss of light olefins via system purging.
摘要翻译： 提供的处理方案和布置提供了用于通过烃裂解加工处理重质烃原料的装置，其中所选择的烃馏分通过基于吸收的产物回收获得，同时通过系统吹扫最小化或避免轻质烯烃的损失。
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公开(公告)号：US08524962B2
公开(公告)日：2013-09-03
申请号：US13013352
申请日：2011-01-25
CPC分类号： C10G29/205 , C10G57/005
摘要： A process for producing a feedstock for gasolines having very little aromatic concentrations is disclosed. The present process uses by-product olefins and alkanes to produce an alkylate for use in gasoline blending.
摘要翻译： 公开了一种生产芳香族浓度很低的汽油的原料的方法。 本发明方法使用副产物烯烃和烷烃来生产用于汽油混合的烷基化物。
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公开(公告)号：US07902412B2
公开(公告)日：2011-03-08
申请号：US11781497
申请日：2007-07-23
CPC分类号： C10G29/205 , C10G57/005
摘要： A process for producing a feedstock for gasolines having very little aromatic concentrations is disclosed. The present process uses by-product olefins and alkanes to produce an alkylate for use in gasoline blending.
摘要翻译： 公开了一种生产芳香族浓度很低的汽油的原料的方法。 本发明方法使用副产物烯烃和烷烃来生产用于汽油混合的烷基化物。
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公开(公告)号：US20110118516A1
公开(公告)日：2011-05-19
申请号：US13013352
申请日：2011-01-25
CPC分类号： C10G29/205 , C10G57/005
摘要： A process for producing a feedstock for gasolines having very little aromatic concentrations is disclosed. The present process uses by-product olefins and alkanes to produce an alkylate for use in gasoline blending.
摘要翻译： 公开了一种生产芳香族浓度很低的汽油的原料的方法。 本发明方法使用副产物烯烃和烷烃来生产用于汽油混合的烷基化物。
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公开(公告)号：US20090030251A1
公开(公告)日：2009-01-29
申请号：US11781497
申请日：2007-07-23
CPC分类号： C10G29/205 , C10G57/005
摘要： A process for producing a feedstock for gasolines having very little aromatic concentrations is disclosed. The present process uses by-product olefins and alkanes to produce an alkylate for use in gasoline blending.
摘要翻译： 公开了一种生产芳香族浓度很低的汽油的原料的方法。 本发明方法使用副产物烯烃和烷烃来生产用于汽油混合的烷基化物。
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公开(公告)号：US09238600B2
公开(公告)日：2016-01-19
申请号：US13325292
申请日：2011-12-14
申请人： David A. Wegerer , Brian W. Hedrick , Zhihao Fei , Daniel N. Myers , Vincenza Myers , Paolo Palmas , Laura E. Leonard
发明人： David A. Wegerer , Brian W. Hedrick , Zhihao Fei , Daniel N. Myers , Paolo Palmas , Laura E. Leonard
CPC分类号： C07C4/06 , C07C2521/04 , C07C2521/08 , C07C2521/16 , C07C2529/40 , C07C2529/50 , C07C2529/65 , C10G11/05 , C10G11/18 , C10G51/026 , C10G2400/20 , Y02P20/52 , Y02P20/584 , C07C11/04 , C07C11/06
摘要： A process for improving the yield of ethylene and propylene from a light naphtha feedstock includes obtaining light naphtha feedstock from a primary cracking zone having a cracking catalyst. The light naphtha feedstock is contacted with an olefin catalyst in an olefin producing zone to produce an ethylene- and propylene-rich stream. After reacting with the olefin catalyst, the ethylene- and propylene-rich stream is separated from the olefin catalyst from in a separator zone. At least a portion of the olefin catalyst is regenerated by combusting coke deposited on a surface of the olefin catalyst in an oxygen-containing environment, and at least a portion of the olefin catalyst is heated. These portions could be the same one or they could be different. In some embodiments, at least a portion of the olefin catalyst could be neither regenerated nor heated. The olefin catalyst is returned to the olefin producing zone.
摘要翻译： 从轻石脑油原料提高乙烯和丙烯的产率的方法包括从具有裂化催化剂的一次裂解区获得轻质石脑油原料。 轻质石脑油原料与烯烃生产区中的烯烃催化剂接触以产生富含乙烯和丙烯的料流。 在与烯烃催化剂反应后，将乙烯和富丙烯物流从分离器区域与烯烃催化剂分离。 至少一部分烯烃催化剂通过在含氧环境中燃烧沉积在烯烃催化剂的表面上的焦炭再生，至少部分烯烃催化剂被加热。 这些部分可以是相同的，也可以是不同的。 在一些实施方案中，烯烃催化剂的至少一部分既不能再生也不能加热。 将烯烃催化剂返回到烯烃生产区。
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8.发明授权Integrated hydrogenation/dehydrogenation reactor in a catalytic reforming process configuration for improved aromatics production 有权在催化重整过程配置中用于改进芳族化合物生产的集成氢化/脱氢反应器公开(公告)号：US09024097B2
公开(公告)日：2015-05-05
申请号：US13327192
申请日：2011-12-15
IPC分类号： C10G35/04 , C07C5/02 , C07C5/41 , C07C15/04 , C07C15/06 , C10G35/085 , C10G35/095 , C10G35/24 , C10G59/02
CPC分类号： C07C5/41 , C07C15/04 , C07C15/06 , C10G35/04 , C10G35/085 , C10G35/095 , C10G35/24 , C10G59/00 , C10G59/02 , C10G69/08 , C10G2400/30
摘要： A process for reforming hydrocarbons is presented. The process involves applying process controls over the reaction temperatures to preferentially convert a portion of the hydrocarbon stream to generate an intermediate stream, which will further react with reduced endothermicity. The intermediate stream is then processed at a higher temperature, where a second reforming reactor is operated under substantially isothermal conditions.
摘要翻译： 介绍了烃类重整方法。 该方法包括对反应温度进行过程控制以优先转化一部分烃流以产生中间流，其将进一步与降低的吸热性反应。 然后在较高温度下处理中间物流，其中第二重整反应器在基本等温条件下操作。
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公开(公告)号：US20130158317A1
公开(公告)日：2013-06-20
申请号：US13327220
申请日：2011-12-15
IPC分类号： C07C15/00
CPC分类号： C07C15/00 , C10G35/00 , C10G59/00 , C10G2400/30
摘要： A process for the production of aromatics through the reforming of a hydrocarbon stream is presented. The process utilizes the differences in properties of components within the hydrocarbon stream to increase the energy efficiency. The differences in the reactions of different hydrocarbon components in the conversion to aromatics allows for different treatments of the different components to reduce the energy used in reforming process.
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公开(公告)号：US20130158310A1
公开(公告)日：2013-06-20
申请号：US13327170
申请日：2011-12-15
IPC分类号： C07C5/42
CPC分类号： C10G59/04 , C10G69/08 , C10G2400/30
摘要： A process for reforming hydrocarbons is presented. The process involves applying process controls over the reaction temperatures to preferentially convert a portion of the hydrocarbon stream to generate an intermediate stream, which will further react with reduced endothermicity. The intermediate stream is then processed at a higher temperature, where a second reforming reactor is operated under substantially isothermal conditions.
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