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    PROCESSES FOR PRODUCING LIGHT OLEFINS
    1.
    发明申请
    PROCESSES FOR PRODUCING LIGHT OLEFINS 有权
    生产光油的方法

    公开(公告)号：US20120123179A1

    公开(公告)日：2012-05-17

    申请号：US13298137

    申请日：2011-11-16

    申请人： Guozhen QI ,  Siqing Zhong ,  Wei Chen ,  Zhinan Yu

    发明人： Guozhen QI ,  Siqing Zhong ,  Wei Chen ,  Zhinan Yu

    IPC分类号： C07C1/24 ,  B01J19/00

    CPC分类号： B01J8/1836 ,  B01J8/005 ,  C07C1/20 ,  C07C2529/85 ,  Y02P20/584 ,  Y02P30/42 ,  C07C11/04 ,  C07C11/06

    摘要： A process for producing light olefins. A feedstock enters a pre-reaction zone and contacts a catalyst comprising at least one silicon-aluminophosphate molecular sieve and produces a gas-phase stream and a catalyst to be regenerated; the gas-phase stream and catalyst to be regenerated enter at least one riser, and the gas-phase stream and catalyst to be regenerated pass from an outlet of the at least one riser and enter a gas-solid rapid separation zone; the separated gas-phase stream enters a separation section; a first portion of the separated catalyst returns to the pre-reaction zone, and a second portion is regenerated in a regenerator; wherein an inlet of the at least one riser extends into the pre-reaction zone, about 60% to about 90% of the height of the at least one riser passes through a heat exchange zone, and the outlet extends into the gas-solid rapid separation zone.

    摘要翻译： 一种生产轻质烯烃的方法。 原料进入预反应区并与包含至少一种硅铝磷酸盐分子筛的催化剂接触并产生气相流和待再生的催化剂; 待再生的气相流和催化剂进入至少一个提升管，并且待再生的气相物流和催化剂从至少一个提升管的出口通过并进入气固快速分离区; 分离的气相流进入分离段; 分离的催化剂的第一部分返回到预反应区，并且第二部分在再生器中再生; 其中所述至少一个提升管的入口延伸到所述预反应区域中，所述至少一个提升管的高度的大约60％至大约90％通过热交换区域，并且所述出口延伸到所述气体 - 固体快速 分离区。

    PROCESS FOR INCREASING ETHYLENE AND/OR PROPYLENE YIELD DURING CONVERSION OF OXYGENATES
    2.
    发明申请
    PROCESS FOR INCREASING ETHYLENE AND/OR PROPYLENE YIELD DURING CONVERSION OF OXYGENATES 有权
    在氧化剂转化期间增加乙烯和/或丙烯醛的方法

    公开(公告)号：US20100331596A1

    公开(公告)日：2010-12-30

    申请号：US12669373

    申请日：2008-07-17

    申请人： Zaiku Xie ,  Guozhen Qi ,  Weimin Yang ,  Siqing Zhong

    发明人： Zaiku Xie ,  Guozhen Qi ,  Weimin Yang ,  Siqing Zhong

    IPC分类号： C07C1/20

    CPC分类号： C07C1/20 ,  C07C2529/85 ,  Y02P20/52 ,  Y02P20/584 ,  Y02P30/42 ,  C07C11/04 ,  C07C11/06

    摘要： The present invention provides a process for increasing ethylene and/or propylene yield during conversion of oxygenates using a system comprising a reactor and a regenerator, wherein the reactor comprises a fluidized bed reactor and a riser reactor, which process increases ethylene and/or propylene yield by using a mixture of the deactivated catalyst from the fluidized bed reactor and the regenerated catalyst from the regenerator in the riser reactor for further cracking the C4+ hydrocarbon stream separated from the product stream.

    摘要翻译： 本发明提供一种使用包含反应器和再生器的系统在含氧化合物转化期间提高乙烯和/或丙烯产率的方法，其中反应器包括流化床反应器和提升管反应器，该方法提高了乙烯和/或丙烯产率 通过使用来自流化床反应器的失活的催化剂和来自提升管反应器中的再生器的再生催化剂的混合物进一步裂化从产物流分离的C4 +烃流。

    Processes for producing light olefins
    3.
    发明授权
    Processes for producing light olefins 有权
    生产轻质烯烃的方法

    公开(公告)号：US08692045B2

    公开(公告)日：2014-04-08

    申请号：US13298137

    申请日：2011-11-16

    申请人： Guozhen Qi ,  Siqing Zhong ,  Wei Chen ,  Zhinan Yu

    发明人： Guozhen Qi ,  Siqing Zhong ,  Wei Chen ,  Zhinan Yu

    IPC分类号： C07C1/24

    CPC分类号： B01J8/1836 ,  B01J8/005 ,  C07C1/20 ,  C07C2529/85 ,  Y02P20/584 ,  Y02P30/42 ,  C07C11/04 ,  C07C11/06

    摘要： A process for producing light olefins is provided. A feedstock enters a pre-reaction zone and contacts a catalyst comprising at least one silicon-aluminophosphate molecular sieve and produces a gas-phase stream; the gas-phase stream and the catalyst enter at least one riser, and the gas-phase stream and the catalyst pass from an outlet of the at least one riser and enter a gas-solid rapid separation zone; the separated gas-phase stream enters a separation section; a first portion of the separated catalyst returns to the pre-reaction zone, and a second portion is regenerated in a regenerator; wherein an inlet of the at least one riser extends into the pre-reaction zone, about 60% to about 90% of the height of the at least one riser passes through a heat exchange zone, and the outlet extends into the gas-solid rapid separation zone.

    摘要翻译： 提供了一种生产轻质烯烃的方法。 原料进入预反应区并与包含至少一个硅铝磷酸盐分子筛的催化剂接触并产生气相流; 所述气相流和所述催化剂进入至少一个提升管，并且所述气相物流和所述催化剂从所述至少一个提升管的出口通过并进入气固快速分离区; 分离的气相流进入分离段; 分离的催化剂的第一部分返回到预反应区，并且第二部分在再生器中再生; 其中所述至少一个提升管的入口延伸到所述预反应区域中，所述至少一个提升管的高度的大约60％至大约90％通过热交换区域，并且所述出口延伸到所述气体 - 固体快速 分离区。

    PROCESS OF PRODUCING LIGHT OLEFINS THROUGH THE CONVERSION OF METHANOL AND ETHANOL
    4.
    发明申请
    PROCESS OF PRODUCING LIGHT OLEFINS THROUGH THE CONVERSION OF METHANOL AND ETHANOL 审中-公开
    通过甲醇和乙醇的转化生产光油的方法

    公开(公告)号：US20100145125A1

    公开(公告)日：2010-06-10

    申请号：US12526408

    申请日：2008-02-04

    申请人： Zaiku Xie ,  Guozhen Qi ,  Huiming Zhang ,  Siqing Zhong

    发明人： Zaiku Xie ,  Guozhen Qi ,  Huiming Zhang ,  Siqing Zhong

    IPC分类号： C07C1/20

    CPC分类号： C07C1/24 ,  Y02P20/52 ,  Y02P30/42 ,  C07C11/04 ,  C07C11/06

    摘要： The present invention discloses a process of producing light olefins through the conversion of methanol and ethanol. The process comprises: feeding a first portion of a feed via a distributor at the bottom of a fluidized-bed reactor to a reaction zone containing a catalyst; feeding a second portion of the feed from at least one location above the distributor to the reaction zone; contacting the feed with the catalyst and allowing it to react, to give a stream containing ethylene and propylene; and withdrawing the stream containing ethylene and propylene from the top of the reactor, and passing it to a separation system to separate ethylene and propylene, wherein the first portion of the feed and the second portion of the feed comprises each independently methanol or ethanol or the both, with a proviso that the total feed comprises both methanol and ethanol, and a weight ratio of methanol to ethanol in the total feed is in a range of from 99:1 to 0.1:1.

    摘要翻译： 本发明公开了通过甲醇和乙醇的转化生产轻质烯烃的方法。 该方法包括：通过流化床反应器底部的分配器将进料的第一部分进料到含有催化剂的反应区; 将进料的第二部分从分配器上方的至少一个位置进料到反应区; 使进料与催化剂接触并使其反应，得到含有乙烯和丙烯的料流; 并从反应器顶部排出含有乙烯和丙烯的料流，并将其送入分离系统以分离乙烯和丙烯，其中进料的第一部分和进料的第二部分各自独立地包括甲醇或乙醇或 两者，条件是总进料包括甲醇和乙醇，并且总进料中甲醇与乙醇的重量比在99:1至0.1:1的范围内。

    Processes for producing light olefins
    5.
    发明授权
    Processes for producing light olefins 有权
    生产轻质烯烃的方法

    公开(公告)号：US09295963B2

    公开(公告)日：2016-03-29

    申请号：US14197450

    申请日：2014-03-05

    申请人： Guozhen Qi ,  Siqing Zhong ,  Wei Chen ,  Zhinan Yu

    发明人： Guozhen Qi ,  Siqing Zhong ,  Wei Chen ,  Zhinan Yu

    IPC分类号： B01J8/18 ,  C07C1/20 ,  B01J8/00

    CPC分类号： B01J8/1836 ,  B01J8/005 ,  C07C1/20 ,  C07C2529/85 ,  Y02P20/584 ,  Y02P30/42 ,  C07C11/04 ,  C07C11/06

    摘要： A process for producing light olefins is provided. A feedstock enters a pre-reaction zone and contacts a catalyst comprising at least one silicon-aluminophosphate molecular sieve and produces a gas-phase stream; the gas-phase stream and the catalyst enter at least one riser, and the gas-phase stream and the catalyst pass from an outlet of the at least one riser and enter a gas-solid rapid separation zone; the separated gas-phase stream enters a separation section; a first portion of the separated catalyst returns to the pre-reaction zone, and a second portion is regenerated in a regenerator; wherein an inlet of the at least one riser extends into the pre-reaction zone, about 60% to about 90% of the height of the at least one riser passes through a heat exchange zone, and the outlet extends into the gas-solid rapid separation zone.

    摘要翻译： 提供了一种生产轻质烯烃的方法。 原料进入预反应区并与包含至少一个硅铝磷酸盐分子筛的催化剂接触并产生气相流; 所述气相流和所述催化剂进入至少一个提升管，并且所述气相物流和所述催化剂从所述至少一个提升管的出口通过并进入气固快速分离区; 分离的气相流进入分离段; 分离的催化剂的第一部分返回到预反应区，并且第二部分在再生器中再生; 其中所述至少一个提升管的入口延伸到所述预反应区域中，所述至少一个提升管的高度的大约60％至大约90％通过热交换区域，并且所述出口延伸到所述气体 - 固体快速 分离区。

    PROCESSES FOR PRODUCING LIGHT OLEFINS
    8.
    发明申请
    PROCESSES FOR PRODUCING LIGHT OLEFINS 审中-公开
    生产光油的方法

    公开(公告)号：US20140186231A1

    公开(公告)日：2014-07-03

    申请号：US14197450

    申请日：2014-03-05

    申请人： Guozhen QI ,  Siqing ZHONG ,  Wei CHEN ,  Zhinan YU

    发明人： Guozhen QI ,  Siqing ZHONG ,  Wei CHEN ,  Zhinan YU

    IPC分类号： B01J8/00

    CPC分类号： B01J8/1836 ,  B01J8/005 ,  C07C1/20 ,  C07C2529/85 ,  Y02P20/584 ,  Y02P30/42 ,  C07C11/04 ,  C07C11/06

    摘要： A process for producing light olefins is provided. A feedstock enters a pre-reaction zone and contacts a catalyst comprising at least one silicon-aluminophosphate molecular sieve and produces a gas-phase stream; the gas-phase stream and the catalyst enter at least one riser, and the gas-phase stream and the catalyst pass from an outlet of the at least one riser and enter a gas-solid rapid separation zone; the separated gas-phase stream enters a separation section; a first portion of the separated catalyst returns to the pre-reaction zone, and a second portion is regenerated in a regenerator; wherein an inlet of the at least one riser extends into the pre-reaction zone, about 60% to about 90% of the height of the at least one riser passes through a heat exchange zone, and the outlet extends into the gas-solid rapid separation zone.

    摘要翻译： 提供了一种生产轻质烯烃的方法。 原料进入预反应区并与包含至少一个硅铝磷酸盐分子筛的催化剂接触并产生气相流; 所述气相流和所述催化剂进入至少一个提升管，并且所述气相物流和所述催化剂从所述至少一个提升管的出口通过并进入气固快速分离区; 分离的气相流进入分离段; 分离的催化剂的第一部分返回到预反应区，并且第二部分在再生器中再生; 其中所述至少一个提升管的入口延伸到所述预反应区域中，所述至少一个提升管的高度的大约60％至大约90％通过热交换区域，并且所述出口延伸到所述气体 - 固体快速 分离区。