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    Process for contacting high contaminated feedstocks with catalyst in an FCC unit
    3.
    发明授权
    Process for contacting high contaminated feedstocks with catalyst in an FCC unit 有权
    将高污染原料与FCC装置中的催化剂接触的方法

    公开(公告)号：US08062506B2

    公开(公告)日：2011-11-22

    申请号：US12814785

    申请日：2010-06-14

    申请人： Brian W. Hedrick ,  Paolo Palmas

    发明人： Brian W. Hedrick ,  Paolo Palmas

    IPC分类号： C10G11/18

    CPC分类号： C10G11/18 ,  C10G2300/202 ,  C10G2400/02 ,  C10G2400/20

    摘要： An FCC process comprising an enlarged riser section and a distributor in an elevated position and with an opening in its tip away from riser walls may reduce coke build-up along the interior walls of a riser. Catalytic mixing may be improved, which could reduce riser coking by increasing hydrocarbon contact with catalyst before contacting the riser wall. Increasing the distance between the introduction of the hydrocarbon and the riser wall may increase this likelihood for hydrocarbon-catalyst contact. Highly contaminated hydrocarbons cause greater coking than do normal hydrocarbons and this FCC process may be effective in decreasing riser coking on such heavy hydrocarbons.

    摘要翻译： 包括扩大的立管部分和升高位置的分配器以及其尖端远离立管壁的开口的FCC方法可以减少沿着提升管的内壁的焦炭积聚。 可以改善催化混合，这可以在接触提升管壁之前通过增加与催化剂的烃接触来减少立管焦化。 增加碳氢化合物和提升管壁之间的距离可能会增加烃 - 催化剂接触的可能性。 高度污染的碳氢化合物比正常碳氢化合物引起更大的焦化，并且该FCC方法可能有效地减少这种重质烃上的立管焦化。

    PROCESS FOR CONTACTING HIGH CONTAMINATED FEEDSTOCKS WITH CATALYST IN AN FCC UNIT
    4.
    发明申请
    PROCESS FOR CONTACTING HIGH CONTAMINATED FEEDSTOCKS WITH CATALYST IN AN FCC UNIT 有权
    在FCC单元中用催化剂接触高污染进料的方法

    公开(公告)号：US20100243529A1

    公开(公告)日：2010-09-30

    申请号：US12814785

    申请日：2010-06-14

    申请人： Brian W. Hedrick ,  Paolo Palmas

    发明人： Brian W. Hedrick ,  Paolo Palmas

    IPC分类号： C10G11/00

    CPC分类号： C10G11/18 ,  C10G2300/202 ,  C10G2400/02 ,  C10G2400/20

    摘要： An FCC process comprising an enlarged riser section and a distributor in an elevated position and with an opening in its tip away from riser walls may reduce coke build-up along the interior walls of a riser. Catalytic mixing may be improved, which could reduce riser coking by increasing hydrocarbon contact with catalyst before contacting the riser wall. Increasing the distance between the introduction of the hydrocarbon and the riser wall may increase this likelihood for hydrocarbon-catalyst contact. Highly contaminated hydrocarbons cause greater coking than do normal hydrocarbons and this FCC process may be effective in decreasing riser coking on such heavy hydrocarbons.

    摘要翻译： 包括扩大的立管部分和升高位置的分配器以及其尖端远离立管壁的开口的FCC方法可以减少沿着提升管的内壁的焦炭积聚。 可以改善催化混合，这可以在接触提升管壁之前通过增加与催化剂的烃接触来减少立管焦化。 增加碳氢化合物和提升管壁之间的距离可能会增加烃 - 催化剂接触的可能性。 高度污染的碳氢化合物比正常碳氢化合物引起更大的焦化，并且该FCC方法可能有效地减少这种重质烃上的立管焦化。

    Device for Contacting High Contaminated Feedstocks with Catalyst in an FCC Unit
    5.
    发明申请
    Device for Contacting High Contaminated Feedstocks with Catalyst in an FCC Unit 有权
    用于在FCC装置中与催化剂接触高污染原料的装置

    公开(公告)号：US20080035526A1

    公开(公告)日：2008-02-14

    申请号：US11463497

    申请日：2006-08-09

    申请人： Brian W. Hedrick ,  Paolo Palmas

    发明人： Brian W. Hedrick ,  Paolo Palmas

    IPC分类号： C10G11/00 ,  B01J8/24

    CPC分类号： C10G11/18 ,  C10G2300/202 ,  C10G2400/02 ,  C10G2400/20

    摘要： An FCC process and apparatus comprising an enlarged riser section and a distributor in an elevated position and with an opening in its tip away from riser walls may reduce coke build-up along the interior walls of a riser. Catalytic mixing may be improved, which could reduce riser coking by increasing hydrocarbon contact with catalyst before contacting the riser wall. Increasing the distance between the introduction of the hydrocarbon and the riser wall may increase this likelihood for hydrocarbon-catalyst contact. Highly contaminated hydrocarbons cause greater coking than do normal hydrocarbons and this FCC process and apparatus may be effective in decreasing riser coking on such heavy hydrocarbons.

    摘要翻译： FCC工艺和设备包括升高部分和升高位置的分配器，并且其尖端远离提升板壁的开口可以沿着提升管的内壁减少焦炭积聚。 可以改善催化混合，这可以在接触提升管壁之前通过增加与催化剂的烃接触来减少立管焦化。 增加碳氢化合物和提升管壁之间的距离可能会增加烃 - 催化剂接触的可能性。 高度污染的碳氢化合物比普通碳氢化合物引起更多的焦化，并且该FCC方法和装置可能有效地减少这种重质烃上的立管焦化。

    Device for contacting high contaminated feedstocks with catalyst in an FCC unit
    6.
    发明授权
    Device for contacting high contaminated feedstocks with catalyst in an FCC unit 有权
    用于将高污染原料与FCC装置中的催化剂接触的装置

    公开(公告)号：US07758817B2

    公开(公告)日：2010-07-20

    申请号：US11463497

    申请日：2006-08-09

    申请人： Brian W. Hedrick ,  Paolo Palmas

    发明人： Brian W. Hedrick ,  Paolo Palmas

    IPC分类号： B01J8/24

    CPC分类号： C10G11/18 ,  C10G2300/202 ,  C10G2400/02 ,  C10G2400/20

    摘要： An FCC process and apparatus comprising an enlarged riser section and a distributor in an elevated position and with an opening in its tip away from riser walls may reduce coke build-up along the interior walls of a riser. Catalytic mixing may be improved, which could reduce riser coking by increasing hydrocarbon contact with catalyst before contacting the riser wall. Increasing the distance between the introduction of the hydrocarbon and the riser wall may increase this likelihood for hydrocarbon-catalyst contact. Highly contaminated hydrocarbons cause greater coking than do normal hydrocarbons and this FCC process and apparatus may be effective in decreasing riser coking on such heavy hydrocarbons.

    摘要翻译： FCC工艺和设备包括升高部分和升高位置的分配器，并且其尖端远离提升板壁的开口可以沿着提升管的内壁减少焦炭积聚。 可以改善催化混合，这可以在接触提升管壁之前通过增加与催化剂的烃接触来减少立管焦化。 增加碳氢化合物和提升管壁之间的距离可能会增加烃 - 催化剂接触的可能性。 高度污染的碳氢化合物比普通碳氢化合物引起更多的焦化，并且该FCC方法和装置可能有效地减少这种重质烃上的立管焦化。

    DUAL RISER CATALYTIC CRACKER FOR INCREASED LIGHT OLEFIN YIELD
    7.
    发明申请
    DUAL RISER CATALYTIC CRACKER FOR INCREASED LIGHT OLEFIN YIELD 有权
    双升式催化裂化器，用于增加光油

    公开(公告)号：US20130158326A1

    公开(公告)日：2013-06-20

    申请号：US13325292

    申请日：2011-12-14

    申请人： David A. Wegerer ,  Brian W. Hedrick ,  Zhihao Fei ,  Paolo Palmas ,  Laura E. Leonard ,  Vincenza Myers

    发明人： David A. Wegerer ,  Brian W. Hedrick ,  Zhihao Fei ,  Daniel N. Myers ,  Paolo Palmas ,  Laura E. Leonard

    IPC分类号： C07C4/06 ,  B01J19/00

    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。

    Dual riser catalytic cracker for increased light olefin yield
    9.
    发明授权
    Dual riser catalytic cracker for increased light olefin yield 有权
    双重提升式催化裂化器，用于提高轻烯烃产率

    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

    IPC分类号： C07C4/06 ,  C10G51/02 ,  C10G11/05 ,  C10G11/18

    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。