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11 条记录 (耗时 0.027 秒)

    Controlling temperature in catalyst regenerators
    3.
    发明授权
    Controlling temperature in catalyst regenerators 有权
    催化剂再生器控制温度

    公开(公告)号：US07452838B2

    公开(公告)日：2008-11-18

    申请号：US11070607

    申请日：2005-03-02

    申请人： Brian A. Cunningham ,  Todd R. Steffens ,  James H. Beech, Jr. ,  Richard E. Walter

    发明人： Brian A. Cunningham ,  Todd R. Steffens ,  James H. Beech, Jr. ,  Richard E. Walter

    IPC分类号： B01J20/34

    CPC分类号： B01J38/32 ,  B01J29/90 ,  B01J38/30 ,  C07C1/20 ,  Y02P20/584 ,  C07C11/02

    摘要： This invention relates to efficiently regenerating catalyst particles by minimizing the formation of localized “hot spots” and “cold spots” in a regeneration zone. In one embodiment, the invention includes mixing spent catalyst from a reactor and cold catalyst from a catalyst cooler in a mixing zone and directing the mixed catalyst to the regeneration zone in a fluidized manner with a fluidizing medium. In the regeneration zone, the mixed catalyst contacts an oxygen-containing regeneration medium under conditions effective to regenerate the spent catalyst contained therein.

    摘要翻译： 本发明涉及通过最小化再生区中局部“热点”和“冷点”的形成来有效地再生催化剂颗粒。 在一个实施方案中，本发明包括将来自反应器的废催化剂和来自混合区域中的催化剂冷却器的冷催化剂混合并将流化介质以流化方式引导至再生区。 在再生区中，混合催化剂在有效地再生其中所含的废催化剂的条件下与含氧再生介质接触。

    HF alkylation process
    4.
    发明申请
    HF alkylation process 审中-公开
    HF烷基化方法

    公开(公告)号：US20080139858A1

    公开(公告)日：2008-06-12

    申请号：US11987428

    申请日：2007-11-30

    申请人： Brian A. Cunningham ,  Ramon A. Strauss ,  Jeffrey M. Fitt

    发明人： Brian A. Cunningham ,  Ramon A. Strauss ,  Jeffrey M. Fitt

    IPC分类号： C07C2/60

    CPC分类号： C07C2/62 ,  C07C7/17 ,  C07C2527/1206 ,  C10G29/205

    摘要： An HF alkylation process for producing gasoline boiling range alkylate product by the alkylation of a light olefin with an isoparaffin in the presence of hydrogen fluoride as an alkylation catalyst, in which the content of organic fluorides in the alkylation product stream is reduced by recontact with additional HF alkylation acid after which the hydrocarbon phase and the denser acid-containing phase are separated in a hydrocyclone. The use of the hydrocyclone enables the acid inventory of the unit to be significantly reduced which still achieving satisfactory removal of the unwanted fluoride by-products.

    摘要翻译： 一种通过在氟化氢作烷基化催化剂存在下，用异链烷烃烷基化轻质烯烃制备汽油沸点烷基化产物的HF烷基化方法，其中烷基化产物流中有机氟化物的含量通过与附加的 HF氢化烷基化酸，之后烃相和更稠的含酸相在水力旋流器中分离。 使用水力旋流器可以显着降低单元的酸存量，这仍然可以令人满意地除去不需要的氟化物副产物。

    Reduced elevation catalyst return line for a fluid catalytic cracking unit
    6.
    发明申请
    Reduced elevation catalyst return line for a fluid catalytic cracking unit 有权
    用于流化催化裂化装置的降低催化剂返回管路

    公开(公告)号：US20090020454A1

    公开(公告)日：2009-01-22

    申请号：US11879259

    申请日：2007-07-17

    申请人： Brian A. Cunningham ,  Christopher G. Smalley ,  Rathna P. Davuluri ,  Dana W. Nouri

    发明人： Brian A. Cunningham ,  Christopher G. Smalley ,  Rathna P. Davuluri ,  Dana W. Nouri

    IPC分类号： C10G11/00 ,  B01D53/00

    CPC分类号： B01J8/0015 ,  C10G11/18 ,  C10G11/182 ,  C10G2300/301

    摘要： The present invention is an improved regenerated catalyst bend assembly for a fluid catalytic cracking unit. In a preferred embodiment, the reduced elevation (“RE-bend” or “REL-bend”) regenerated catalyst return line assembly of the present invention has an outlet elevation that is lower than the inlet elevation of the RE-bend or REL-bend regenerated catalyst return line assembly, and a process for utilizing the assembly in a fluid catalytic cracking unit. The present invention is especially useful in the modification of existing fluid catalytic cracking units to lower the elevation of the outlet of the regenerated catalyst return line assembly, thereby providing needed space to increase the fluid catalytic cracking reactor riser length.

    摘要翻译： 本发明是用于流化催化裂化装置的改进的再生催化剂弯曲组件。 在优选实施例中，本发明的再生催化剂返回管线组件的缩小的高度（“RE-弯曲”或“REL-弯曲”）具有低于RE弯头或REL-弯头的入口高度的出口高度 再生催化剂返回管路组件，以及在流化催化裂化装置中利用该组件的方法。 本发明特别可用于改进现有的流化催化裂化装置以降低再生催化剂返回管线组件的出口的高度，从而提供所需的空间以增加流化催化裂化反应器提升管的长度。

    HF akylation process
    7.
    发明申请
    HF akylation process 审中-公开
    HF烷基化方法

    公开(公告)号：US20090221863A1

    公开(公告)日：2009-09-03

    申请号：US12320400

    申请日：2009-01-26

    申请人： Ramon A. Strauss ,  Brian A. Cunningham ,  Jeffrey M. Fitt ,  Ramesh R. Hemrajani

    发明人： Ramon A. Strauss ,  Brian A. Cunningham ,  Jeffrey M. Fitt ,  Ramesh R. Hemrajani

    IPC分类号： C07C2/60 ,  B01J14/00

    CPC分类号： C07C2/62 ,  C07C2527/1206 ,  C10L1/06

    摘要： An HF alkylation process for producing gasoline boiling range alkylate product by the alkylation of a light olefin with an isoparaffin in the presence of hydrogen fluoride as an alkylation catalyst, in which the content of organic fluorides in the alkylation product stream is reduced by recontact with additional HF alkylation acid after which the hydrocarbon phase and the denser acid-containing phase are separated in a hydrocyclone. The use of the hydrocyclone enables the acid inventory of the unit to be significantly reduced which still achieving satisfactory removal of the unwanted fluoride by-products.

    摘要翻译： 一种通过在氟化氢作烷基化催化剂存在下，用异链烷烃烷基化轻质烯烃制备汽油沸点烷基化产物的HF烷基化方法，其中烷基化产物流中有机氟化物的含量通过与附加的 HF氢化烷基化酸，之后烃相和更稠的含酸相在水力旋流器中分离。 使用水力旋流器可以显着降低单元的酸存量，这仍然可以令人满意地除去不需要的氟化物副产物。

    Reduced elevation catalyst return line for a fluid catalytic cracking unit
    8.
    发明授权
    Reduced elevation catalyst return line for a fluid catalytic cracking unit 有权
    用于流化催化裂化装置的降低催化剂返回管路

    公开(公告)号：US08202412B2

    公开(公告)日：2012-06-19

    申请号：US11879259

    申请日：2007-07-17

    申请人： Brian A. Cunningham ,  Christopher G. Smalley ,  Rathna P. Davuluri ,  Dana W. Nouri

    发明人： Brian A. Cunningham ,  Christopher G. Smalley ,  Rathna P. Davuluri ,  Dana W. Nouri

    IPC分类号： C10G11/00 ,  B01J8/18

    CPC分类号： B01J8/0015 ,  C10G11/18 ,  C10G11/182 ,  C10G2300/301

    摘要： The present invention is an improved regenerated catalyst bend assembly for a fluid catalytic cracking unit. In a preferred embodiment, the reduced elevation (“RE-bend” or “REL-bend”) regenerated catalyst return line assembly of the present invention has an outlet elevation that is lower than the inlet elevation of the RE-bend or REL-bend regenerated catalyst return line assembly, and a process for utilizing the assembly in a fluid catalytic cracking unit. The present invention is especially useful in the modification of existing fluid catalytic cracking units to lower the elevation of the outlet of the regenerated catalyst return line assembly, thereby providing needed space to increase the fluid catalytic cracking reactor riser length.

    摘要翻译： 本发明是用于流化催化裂化装置的改进的再生催化剂弯曲组件。 在优选实施例中，本发明的再生催化剂返回管线组件的缩小的高度（“RE-弯曲”或“REL-弯曲”）具有低于RE弯头或REL-弯头的入口高度的出口高度 再生催化剂返回管路组件，以及在流化催化裂化装置中利用该组件的方法。 本发明特别可用于改进现有的流化催化裂化装置以降低再生催化剂返回管线组件的出口的高度，从而提供所需的空间以增加流化催化裂化反应器提升管的长度。

    Sulfuric acid alkylation reactor system with static mixers
    10.
    发明授权
    Sulfuric acid alkylation reactor system with static mixers 失效
    具有静态混合器的硫酸烷基化反应器系统

    公开(公告)号：US5785933A

    公开(公告)日：1998-07-28

    申请号：US779290

    申请日：1997-01-21

    申请人： Brian A. Cunningham ,  Saverio G. Greco

    发明人： Brian A. Cunningham ,  Saverio G. Greco

    IPC分类号： B01F3/08 ,  B01F5/00

    CPC分类号： B01J4/005 ,  B01J14/00 ,  B01J19/006 ,  B01J19/2465 ,  B01J4/004 ,  C10G29/205 ,  B01F5/0062 ,  B01J2219/00006 ,  B01J2219/00182 ,  B01J2219/00765

    摘要： A sulfuric acid-catalyzed alkylation reactor system is provided for alkylating isoparaffins with olefins to produce hydrocarbon alkylates. The reactor vessel has a vertical cylindrical wall, a top, an inverted conical bottom portion, internal perforated baffles and multiple emulsion injection inlet pipes, disposed tangentially to and communicating with the interior of the reactor vessel. The emulsion injection inlet pipes have static mixers incorporated therein and tangential injection of the emulsion imparts a circular motion to the contents of the reactor vessel, resulting in partial phase separation of the reacted products. The reactor vessel communicates with a settling vessel through a transfer pipe having a vertical portion suspended within the central portion of the reactor vessel and a horizontal portion sealably extending through the cylindrical wall of the reactor vessel. The transfer pipe has a first end near the conical bottom portion of the reactor vessel and a second end at a top portion of the settling vessel. The reactor system enables a sulfuric-acid catalyzed reaction of olefins with isoparaffins utilizing static mixing of the reactants, and minimizing leakage of the reactants to the environment.

    摘要翻译： 提供硫酸催化的烷基化反应器系统用于使烯烃与异链烷烃烷基化以产生烃烷基化物。 反应器容器具有垂直的圆柱形壁，顶部，倒锥形底部部分，内部穿孔挡板和多个乳液注入入口管道，其与反应器容器的内部相切地设置并与其连通。 乳液注射入口管具有并入其中的静态混合器，并且乳液的切向注入向反应器容器的内容物施加圆周运动，导致反应产物的部分相分离。 反应器容器通过具有悬挂在反应器容器的中心部分中的垂直部分的输送管和与反应容器的圆筒壁密封地延伸的水平部分与沉降容器连通。 输送管具有在反应器容器的锥形底部附近的第一端和在沉降容器的顶部的第二端。 反应器系统使得烯烃与异链烷烃的硫酸催化反应利用反应物的静态混合，并且使反应物对环境的泄漏最小化。