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    FLUIDIZED CATALYTIC PROCESS FOR PRODUCTION OF DIMETHYL ETHER FROM METHANOL
    1.
    发明申请
    FLUIDIZED CATALYTIC PROCESS FOR PRODUCTION OF DIMETHYL ETHER FROM METHANOL 有权
    用于从甲醇生产二甲醚的流化催化方法

    公开(公告)号：US20100076227A1

    公开(公告)日：2010-03-25

    申请号：US12594006

    申请日：2008-03-27

    申请人： Zheng Li ,  Qiang Fu ,  Chaogang Xie ,  Minggang Li ,  Anguo Mao ,  Lisheng Li ,  Genquan Zhu ,  Fengmei Zhang ,  Yinbin Luo

    发明人： Zheng Li ,  Qiang Fu ,  Chaogang Xie ,  Minggang Li ,  Anguo Mao ,  Lisheng Li ,  Genquan Zhu ,  Fengmei Zhang ,  Yinbin Luo

    IPC分类号： C07C41/09

    CPC分类号： B01J29/90 ,  B01J29/005 ,  B01J29/088 ,  B01J29/46 ,  B01J29/85 ,  B01J2229/42 ,  C07C41/09 ,  Y02P20/584 ,  Y02P20/588 ,  C07C43/043

    摘要： The present invention provides a fluidized catalytic process for production of dimethyl ether from methanol, wherein said process is carried out in a reactor in which the catalyst is in a fluidized state. Said process comprises the following steps of (1) feeding the methanol feedstock via two or more locations selected from the bottom, lower part, middle part and upper part of the reactor, contacting with the catalyst for preparation of dimethyl ether by methanol dehydration, carrying out the reaction of preparing dimethyl ether by methanol dehydration to obtain the reaction stream, separating said reaction stream to obtain a coked catalyst and a crude product primarily containing the target product, i.e. dimethyl ether; (2) totally or partially feeding the coked catalyst obtained in step (1) into a regenerator in a continuous or batch manner for regeneration via coke-burning, the regenerated catalyst being directly recycled to step (1) after being totally or partially cooled.

    摘要翻译： 本发明提供了一种用于从甲醇生产二甲醚的流化催化方法，其中所述方法在催化剂处于流化状态的反应器中进行。 所述方法包括以下步骤：（1）经由选自反应器的底部，底部，中部和上部的两个或多个位置进料甲醇原料，与甲醇脱水制备二甲醚的催化剂接触，携带 通过甲醇脱水制备二甲醚以获得反应流的反应，分离所述反应流，得到主要含有目标产物（即二甲醚）的焦化催化剂和粗产物; （2）将在步骤（1）中获得的焦化催化剂全部或部分地以连续或间歇方式进料到再生器中，以通过焦炭燃烧再生，再生催化剂在全部或部分冷却后直接再循环到步骤（1）。

    Fluidized catalytic process for production of dimethyl ether from methanol
    2.
    发明授权
    Fluidized catalytic process for production of dimethyl ether from methanol 有权
    用于从甲醇生产二甲醚的流化催化方法

    公开(公告)号：US08304582B2

    公开(公告)日：2012-11-06

    申请号：US12594006

    申请日：2008-03-27

    申请人： Zheng Li ,  Qiang Fu ,  Chaogang Xie ,  Minggang Li ,  Anguo Mao ,  Lisheng Li ,  Genquan Zhu ,  Fengmei Zhang ,  Yi bin Luo

    发明人： Zheng Li ,  Qiang Fu ,  Chaogang Xie ,  Minggang Li ,  Anguo Mao ,  Lisheng Li ,  Genquan Zhu ,  Fengmei Zhang ,  Yi bin Luo

    IPC分类号： C07C41/09 ,  C07C43/04 ,  F27B15/08

    CPC分类号： B01J29/90 ,  B01J29/005 ,  B01J29/088 ,  B01J29/46 ,  B01J29/85 ,  B01J2229/42 ,  C07C41/09 ,  Y02P20/584 ,  Y02P20/588 ,  C07C43/043

    摘要： The present invention provides a fluidized catalytic process for production of dimethyl ether from methanol, wherein said process is carried out in a reactor in which the catalyst is in a fluidized state. Said process comprises the following steps of (1) feeding the methanol feedstock via two or more locations selected from the bottom, lower part, middle part and upper part of the reactor, contacting with the catalyst for preparation of dimethyl ether by methanol dehydration, carrying out the reaction of preparing dimethyl ether by methanol dehydration to obtain the reaction stream, separating said reaction stream to obtain a coked catalyst and a crude product primarily containing the target product, i.e. dimethyl ether; (2) totally or partially feeding the coked catalyst obtained in step (1) into a regenerator in a continuous or batch manner for regeneration via coke-burning, the regenerated catalyst being directly recycled to step (1) after being totally or partially cooled.

    摘要翻译： 本发明提供了一种用于从甲醇生产二甲醚的流化催化方法，其中所述方法在催化剂处于流化状态的反应器中进行。 所述方法包括以下步骤：（1）经由选自反应器的底部，底部，中部和上部的两个或多个位置进料甲醇原料，与甲醇脱水制备二甲醚的催化剂接触，携带 通过甲醇脱水制备二甲醚以获得反应流的反应，分离所述反应流，得到主要含有目标产物（即二甲醚）的焦化催化剂和粗产物; （2）将在步骤（1）中获得的焦化催化剂全部或部分地以连续或间歇方式进料到再生器中，以通过焦炭燃烧再生，再生催化剂在全部或部分冷却后直接再循环到步骤（1）。

    Catalytic cracking process for increasing simultaneously the yields of diesel oil and liquefied gas
    9.
    发明授权
    Catalytic cracking process for increasing simultaneously the yields of diesel oil and liquefied gas 有权
    催化裂化过程同时提高柴油和液化气的产率

    公开(公告)号：US06416656B1

    公开(公告)日：2002-07-09

    申请号：US09602568

    申请日：2000-06-22

    申请人： Jiushun Zhang ,  Anguo Mao ,  Xiaoxiang Zhong ,  Zhigang Zhang ,  Zubi Chen ,  Yamin Wang ,  Wei Wang ,  Shuxin Cui ,  Zeyu Wang ,  Hua Cui ,  Ruichi Zhang

    发明人： Jiushun Zhang ,  Anguo Mao ,  Xiaoxiang Zhong ,  Zhigang Zhang ,  Zubi Chen ,  Yamin Wang ,  Wei Wang ,  Shuxin Cui ,  Zeyu Wang ,  Hua Cui ,  Ruichi Zhang

    IPC分类号： C10G1100

    CPC分类号： C10G11/18

    摘要： This discloses a process for catalytically cracking hydrocarbon stocks in a riser or fluidized bed reactor simultaneously to increase yields of diesel and liquefied gas. The process includes the steps of: first, charging a gasoline stock and a catalytic cracking catalyst into a lower zone of the reactor to permit contact between the catalyst and the gasoline stock and to produce a liquefied gas-rich oil-gas mixture containing reacted catalyst. The resulting liquefied gas-rich oil-gas mixture (still containing reacted catalyst) is then introduced into a reaction zone above the lower zone of the reactor. Simultaneously, at least one conventional catalytic cracking hydrocarbon feed is also fed independently into at least two sites is situated at a different height above the lower zone of the reactor. The resulting mixture is then separated in a conventional fashion.

    摘要翻译： 这公开了一种在提升管或流化床反应器中同时催化裂化烃原料以提高柴油和液化气的产率的方法。 该方法包括以下步骤：首先，将汽油原料和催化裂化催化剂装入反应器的下部区域，以允许催化剂和汽油原料之间的接触，并产生含有反应催化剂的液化气体富含油气混合物 。 然后将所得到的液化气体富含油气混合物（仍含有反应催化剂）引入到反应器下部区域上方的反应区。 同时，至少一种常规的催化裂化烃进料也独立地进料到至少两个位置，位于反应器下部区域上方的不同高度处。 然后将所得混合物以常规方式分离。