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    Reactor cooler
    11.
    发明申请
    Reactor cooler 审中-公开
    反应堆冷却器

    公开(公告)号：US20090163756A1

    公开(公告)日：2009-06-25

    申请号：US12002814

    申请日：2007-12-19

    Applicant: Peter R. Pujado

    Inventor： Peter R. Pujado

    IPC: C07C1/00 ,  B01J19/00 ,  F28D15/00

    CPC classification number: B01J8/1854 ,  B01J8/1836 ,  B01J2208/00132 ,  C07C1/20 ,  C10G2400/20 ,  F28D7/06 ,  F28D13/00 ,  C07C11/02

    Abstract: A reactor for converting a feedstream having one or more oxygenated compounds to a product containing olefins is provided. The reactor comprises a fluidized reaction zone defined by a reactor wall and a feedstream inlet located adjacent the reaction zone. The feedstream inlet is operative to feed the reaction zone with said feedstream. A riser extends from said reaction zone and carries a vaporized combination of said feedstream and said catalyst from said reaction zone to a disengaging zone fed by the riser. At least one cooling tube is disposed within the reactor and extends substantially vertically and substantially parallel to the reactor wall. The cooling tube is located adjacent the reactor wall and extends from an upper portion of the reaction zone towards a lower portion of the reaction zone. Also provided is a cooling system for a methanol to olefin reactor. Finally, a method of producing olefins from a feedstream having an oxygenate is provided. The method includes cooling the reaction which produces olefins from the oxygenate feedstream.

    Abstract translation: 提供了一种用于将具有一种或多种含氧化合物的进料流转化为含有烯烃的产物的反应器。 反应器包括由反应器壁和邻近反应区定位的进料流入口限定的流化反应区。 进料流入口可操作以与所述原料流一起进料反应区。 提升管从所述反应区延伸并将所述进料流和所述催化剂的蒸发组合从所述反应区运送到由提升管供给的分离区。 至少一个冷却管设置在反应器内并基本上垂直且基本平行于反应器壁延伸。 冷却管位于反应器壁附近并且从反应区的上部朝向反应区的下部延伸。 还提供了用于甲醇至烯烃反应器的冷却系统。 最后，提供了从具有含氧化合物的原料流生产烯烃的方法。 该方法包括冷却从含氧物进料流产生烯烃的反应。

    Falling film reactor with corrugated plates
    13.
    发明授权
    Falling film reactor with corrugated plates 失效
    具有波纹板的落膜反应堆

    公开(公告)号：US06596244B1

    公开(公告)日：2003-07-22

    申请号：US09316714

    申请日：1999-05-21

    Applicant: Peter R. Pujado

    Inventor： Peter R. Pujado

    IPC: B01D122

    CPC classification number: C07C303/06 ,  B01J10/02 ,  B01J19/247 ,  B01J19/32 ,  B01J2219/3221 ,  B01J2219/32213 ,  B01J2219/3222 ,  B01J2219/32227 ,  B01J2219/32244 ,  C07C309/04

    Abstract: An arrangement for a falling film type reactor uses corrugated plates to improve the distribution and dispersion of the gaseous reactant into the liquid. Corrugated plates introduce increased turbulence for promoting better distribution and dispersion of the gas. Corrugation angles can be varied to suit the fluid flow properties of the liquid reactant. The reactor arrangement can also include heat transfer channels defined by the corrugated plates in an alternate arrangement of heat transfer channels and gas liquid contacting channels. The corrugations may also be varied to suit the particular heat transfer requirements of the reactions. The corrugated plates are spaced apart in the contacting channels to prevent localized film contact and placed in contact in the heat exchange portion to stabilize the plate elements defining the corrugations.

    Abstract translation: 降膜型反应器的布置使用波纹板来改善气态反应物在液体中的分布和分散。 波纹板引起增加的湍流，以促进气体的更好分布和分散。 可以改变波纹角以适应液体反应物的流体流动性质。 反应器装置还可以包括由传热通道和气液接触通道的替代布置的波纹板限定的传热通道。 波纹也可以变化以适应反应的特定传热要求。 波纹板在接触通道中间隔开以防止局部膜接触并且置于接触热交换部分中以稳定限定波纹的板元件。

    Preparing a light-olefin containing product stream from an oxygenate-containing feed steam using reactors directing a flow of a fluidized dual-function catalyst system
    16.
    发明授权
    Preparing a light-olefin containing product stream from an oxygenate-containing feed steam using reactors directing a flow of a fluidized dual-function catalyst system 有权
    使用引导流化双功能催化剂体系流的反应器从含氧化合物的进料蒸汽制备含轻烯烃的产物流

    公开(公告)号：US08735639B2

    公开(公告)日：2014-05-27

    申请号：US12755632

    申请日：2010-04-07

    Applicant: Andrea G. Bozzano ,  Bryan K. Glover ,  Peter R. Pujado

    Inventor： Andrea G. Bozzano ,  Bryan K. Glover ,  Peter R. Pujado

    IPC: B01J8/00 ,  C07C2/00

    CPC classification number: C07C11/06 ,  C07C1/20 ,  C07C4/06 ,  C07C2529/40 ,  C07C2529/85

    Abstract: The present process provides a method for converting an oxygenate-containing feed stream to an olefin-containing product stream. The method includes: (1) providing a first fluidized catalytic reactor for converting methanol to propylene, the first reactor having a fluidized catalyst system comprising a first catalyst and a second catalyst; (2) providing a second fluidized catalytic reactor communicating with the first fluidized catalytic reactor for cracking heavy olefins having four carbon atoms or greater into propylene, the second reactor having the fluidized catalyst system; (3) providing an oxygenate containing feed to the first reactor; and (4) fluidizing the catalyst system with the oxygenate containing feed.

    Abstract translation: 本发明方法提供了将含氧化合物的进料流转化为含烯烃的产物流的方法。 该方法包括：（1）提供用于将甲醇转化为丙烯的第一流化催化反应器，所述第一反应器具有包含第一催化剂和第二催化剂的流化催化剂体系; （2）提供与第一流化催化反应器连通的第二流化催化反应器，用于将具有四个或更多碳原子的重质烯烃裂解成丙烯，第二反应器具有流化催化剂体系; （3）向第一反应器提供含氧化合物进料; 和（4）用含氧化合物进料使催化剂体系流化。

    Process for enhanced olefin production
    17.
    发明授权
    Process for enhanced olefin production 有权
    烯烃生产增强工艺

    公开(公告)号：US07803330B2

    公开(公告)日：2010-09-28

    申请号：US11874448

    申请日：2007-10-18

    Applicant: Bipin V. Vora ,  Peter R. Pujado

    Inventor： Bipin V. Vora ,  Peter R. Pujado

    IPC: B01J8/04

    CPC classification number: C07C1/20 ,  C07C4/06 ,  C07C2529/035 ,  C07C2529/40 ,  C07C2529/86 ,  Y02P30/42 ,  C07C11/06 ,  C07C11/04

    Abstract: The present invention relates to a process for the production of light weight olefins comprising olefins having from 2 to 3 carbon atoms per molecule from an oxygenate feedstock. The process comprises passing the oxygenate feedstock to an oxygenate conversion zone containing a metal aluminophosphate catalyst to produce a light weight olefin stream. A propylene stream and/or mixed butylene is fractionated from said light weight olefin stream and a medium weight C4 to C7 stream is cracked in a separate olefin cracking reactor to enhance the yield of ethylene and propylene products.

    Abstract translation: 本发明涉及一种生产轻质烯烃的方法，其包含每分子含有2-3个碳原子的含氧原料。 该方法包括使含氧化合物原料通入含有金属磷酸铝催化剂的含氧化合物转化区以产生轻质烯烃物流。 将丙烯料流和/或混合丁烯从所述轻质烯烃料流中分馏，并将中等重量的C 4至C 7流在单独的烯烃裂解反应器中裂化，以提高乙烯和丙烯产物的产率。

    Preparing A Light-Olefin Containing Product Stream from an Oxygenate-Containing Feed Steam Using Reactors Directing a Flow of a Fluidized Dual-Function Catalyst System
    18.
    发明申请
    Preparing A Light-Olefin Containing Product Stream from an Oxygenate-Containing Feed Steam Using Reactors Directing a Flow of a Fluidized Dual-Function Catalyst System 有权
    使用引导流化双功能催化剂体系流动的反应器，从含氧化合物的进料蒸汽制备含有轻烯烃的轻质烯烃

    公开(公告)号：US20100204530A1

    公开(公告)日：2010-08-12

    申请号：US12755632

    申请日：2010-04-07

    Applicant: Andrea G. Bozzano ,  Bryan K. Glover ,  Peter R. Pujado

    Inventor： Andrea G. Bozzano ,  Bryan K. Glover ,  Peter R. Pujado

    IPC: C07C1/20

    CPC classification number: C07C11/06 ,  C07C1/20 ,  C07C4/06 ,  C07C2529/40 ,  C07C2529/85

    Abstract: The present invention provides a reactor system for converting an oxygenate-containing feed stream to an olefin-containing product stream. The system includes: (1) a first fluidized catalytic reactor for converting methanol to propylene, the first reactor having a fluidized catalyst system comprising a first catalyst and a second catalyst; (2) a second fluidized catalytic reactor communicating with the first fluidized catalytic reactor for cracking heavy olefins having four carbon atoms or greater into propylene, the second reactor having the fluidized catalyst system; (3) wherein the first catalyst is a non-zeolite molecular sieve catalyst; and (4) wherein the second catalyst is a zeolite molecular sieve catalyst.

    Abstract translation: 本发明提供了一种用于将含氧化合物的进料流转化为含烯烃的产物流的反应器系统。 该系统包括：（1）用于将甲醇转化成丙烯的第一流化催化反应器，所述第一反应器具有包含第一催化剂和第二催化剂的流化催化剂体系; （2）与第一流化催化反应器连通的第二流化催化反应器，用于将具有四个或更多碳原子的重质烯烃裂解成丙烯，第二反应器具有流化催化剂体系; （3）其中第一催化剂是非沸石分子筛催化剂; 和（4）其中第二催化剂是沸石分子筛催化剂。

    Process for enhanced olefin production
    19.
    发明授权
    Process for enhanced olefin production 有权
    烯烃生产增强工艺

    公开(公告)号：US07317133B2

    公开(公告)日：2008-01-08

    申请号：US10302258

    申请日：2002-11-21

    Applicant: Bipin V. Vora ,  Peter R. Pujado

    Inventor： Bipin V. Vora ,  Peter R. Pujado

    IPC: C07C4/02 ,  C07C1/20

    CPC classification number: C07C1/20 ,  C07C4/06 ,  C07C2529/035 ,  C07C2529/40 ,  C07C2529/86 ,  Y02P30/42 ,  C07C11/06 ,  C07C11/04

    Abstract: The present invention relates to a process for the production of light weight olefins comprising olefins having from 2 to 3 carbon atoms per molecule from an oxygenate feedstock. The process comprises passing the oxygenate feedstock to an oxygenate conversion zone containing a metal alumino phosphate catalyst to produce a light weight olefin stream. A propylene stream and/or mixed butylene is fractionated from said light weight olefin stream and a medium weight C4 to C7 stream is cracked in a separate olefin cracking reactor to enhance the yield of ethylene and propylene products.

    Abstract translation: 本发明涉及一种生产轻质烯烃的方法，其包含每分子含有2-3个碳原子的含氧原料。 该方法包括使含氧化合物原料通入含有金属磷酸铝催化剂的含氧化合物转化区以产生轻质烯烃流。 将丙烯料流和/或混合的丁烯从所述轻质烯烃料流中分馏，并将中等重量C 4至C 7 H 2流在单独的烯烃裂解反应器中裂化以增强 乙烯和丙烯产品的产率。

    Catalytic distillation with in situ catalyst replacement
    20.
    发明授权
    Catalytic distillation with in situ catalyst replacement 失效
    催化蒸馏原位催化剂更换

    公开(公告)号：US06299845B1

    公开(公告)日：2001-10-09

    申请号：US08907728

    申请日：1997-08-08

    Applicant: Jacques J. L. Romatier ,  Peter R. Pujado

    Inventor： Jacques J. L. Romatier ,  Peter R. Pujado

    IPC: B01J802

    CPC classification number: B01J8/12 ,  B01D3/009 ,  B01J8/0035 ,  B01J8/02 ,  B01J8/087 ,  B01J19/32 ,  B01J2208/022 ,  B01J2219/3221 ,  B01J2219/32213 ,  B01J2219/32237 ,  B01J2219/32466 ,  B01J2219/32475 ,  B01J2219/3306

    Abstract: A catalytic distillation packing that has continuous smooth channels over its entire length is used to change out catalyst in a catalyst distillation arrangement without replacement of packing units and long turnaround times. The long, continuous channels are formed from perforated, corrugated plates that have a sufficient thickness to maintain the geometry of the channels and permit free catalyst flow for catalyst change out. The thickness of the plates also eliminates the need for complicated bracing and attachment arrangements that adds to the expense of the packing arrangement and can obstruct the movement of catalyst therethrough. The long, continuous channels are used with an inlet arrangement that provides ready adjustment of the number of channels that are filled with catalyst and channels that are free of catalyst. It is also possible in this arrangement to operate with a channel arrangement wherein all channels are filled with catalyst.

    Abstract translation: 在整个长度上具有连续平滑通道的催化蒸馏填料用于在催化剂蒸馏装置中改变催化剂，而不需要更换包装单元和长的周转时间。 长的连续通道由穿孔的波纹板形成，其具有足够的厚度以保持通道的几何形状，并允许催化剂流出以释放催化剂。 板的厚度也消除了复杂的支撑和附接布置的需要，这增加了填充布置的费用并且可以阻碍催化剂通过其运动。 长的连续通道与入口装置一起使用，其提供了填充有不含催化剂的催化剂和通道的通道数量的准备调整。 在这种布置中也可以以通道布置操作，其中所有通道都填充有催化剂。

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