TURNDOWN THERMOCOMPRESSOR DESIGN FOR CONTINUOUS CATALYST RECOVERY
    1.
    发明申请
    TURNDOWN THERMOCOMPRESSOR DESIGN FOR CONTINUOUS CATALYST RECOVERY 有权
    用于连续催化剂恢复的预热式热电偶设计

    公开(公告)号:US20100222202A1

    公开(公告)日:2010-09-02

    申请号:US12394108

    申请日:2009-02-27

    IPC分类号: B01J20/34

    摘要: Systems and processes for regenerating catalyst are provided herein that include a catalyst regeneration tower having a cooling zone that receives a catalyst cooling stream generated by a cooling gas loop. The systems and processes include a first thermocompressor that utilizes a first motive vapor and a second thermocompressor that utilizes a second motive vapor in order to provide the catalyst cooling stream to the regeneration tower. The second thermocompressor operates in parallel with the first thermocompressor. The first thermocompressor can utilize combustion air as the motive vapor. The second thermocompressor can utilize nitrogen as the motive vapor.

    摘要翻译: 本文提供了用于再生催化剂的系统和方法,其包括催化剂再生塔,其具有接收由冷却气体回路产生的催化剂冷却流的冷却区。 系统和方法包括利用第一动力蒸汽的第一热压机和利用第二动力蒸汽的第二热压机,以便向再生塔提供催化剂冷却流。 第二个热压机与第一个热压机平行运行。 第一个热压机可以利用燃烧空气作为动力蒸汽。 第二个热压机可以利用氮气作为动力蒸汽。

    Process for controlling a fluidized bed combustion zone and its use
    4.
    发明申请
    Process for controlling a fluidized bed combustion zone and its use 有权
    控制流化床燃烧区及其用途的方法

    公开(公告)号:US20050074369A1

    公开(公告)日:2005-04-07

    申请号:US10640578

    申请日:2003-08-14

    申请人: Sanchez Eric

    发明人: Sanchez Eric

    摘要: Process for controlling the combustion zone of a fluidized bed process comprising a regeneration zone and a reaction zone, the catalyst circulating between these two zones, and the regeneration zone comprising a combustion stage of the coke deposited on the catalyst in the reaction zone, control of the combustion zone being performed on the basis of a characteristic variable of the operation of said combustion zone, said characteristic variable being the object of automatic regulation by acting on the catalyst throughput, characterized in that the value of the catalyst throughput or of any control variable connected unequivocally to the catalyst is determined based on information on the operating values of the combustion zone, at least one of which corresponds to an independent evaluation of the level of coke deposited on the catalyst.

    摘要翻译: 用于控制流化床方法的燃烧区的方法,该流化床方法包括再生区和反应区,在这两个区之间循环的催化剂,再生区包括沉积在反应区催化剂上的焦炭燃烧阶段,控制 所述燃烧区域是基于所述燃烧区域的操作的特征变量进行的,所述特征变量是通过作用于催化剂生产量的自动调节的对象,其特征在于催化剂生产量或任何控制变量 基于关于燃烧区的操作值的信息确定催化剂的明确连接,其中至少一个对应于沉积在催化剂上的焦炭水平的独立评估。

    Systems and Methods for Regenerating A Spent Catalyst
    7.
    发明申请
    Systems and Methods for Regenerating A Spent Catalyst 有权
    再生废催化剂的系统和方法

    公开(公告)号:US20110251046A1

    公开(公告)日:2011-10-13

    申请号:US12757554

    申请日:2010-04-09

    IPC分类号: B01J38/12

    摘要: Systems and methods for regenerating a spent catalyst are provided. The method can include heating a hydrocarbon and a coke precursor in the presence of catalyst particles to provide a cracked hydrocarbon product and coked catalyst particles. The cracked hydrocarbon product and the coked catalyst particles can be selectively separated to provide a hydrocarbon product and coked catalyst particles. The coked catalyst particles can be mixed with a carrier fluid to provide a mixture. The mixture can be introduced to an upper surface of a dense phase catalyst zone disposed within a regenerator. A gas can be introduced to a lower zone of the dense phase catalyst zone. At least a portion of the carbon deposited on the coked catalyst particles can be combusted to provide a flue gas, heat, and a regenerated catalyst.

    摘要翻译: 提供了用于再生废催化剂的系统和方法。 该方法可以包括在催化剂颗粒存在下加热烃和焦炭前体以提供裂化的烃产物和焦化的催化剂颗粒。 裂化的烃产物和焦化的催化剂颗粒可以选择性分离以提供烃产物和焦化的催化剂颗粒。 焦化的催化剂颗粒可与载体流体混合以提供混合物。 可以将混合物引入设置在再生器内的致密相催化剂区的上表面。 可以将气体引入密相催化剂区的下部区域。 沉积在焦化催化剂颗粒上的碳的至少一部分可以燃烧以提供烟道气,热和再生催化剂。

    Systems and methods for regenerating a spent catalyst
    10.
    发明授权
    Systems and methods for regenerating a spent catalyst 有权
    用于再生废催化剂的系统和方法

    公开(公告)号:US08618011B2

    公开(公告)日:2013-12-31

    申请号:US12757554

    申请日:2010-04-09

    摘要: Systems and methods for regenerating a spent catalyst are provided. The method can include heating a hydrocarbon and a coke precursor in the presence of catalyst particles to provide a cracked hydrocarbon product and coked catalyst particles. The cracked hydrocarbon product and the coked catalyst particles can be selectively separated to provide a hydrocarbon product and coked catalyst particles. The coked catalyst particles can be mixed with a carrier fluid to provide a mixture. The mixture can be introduced to an upper surface of a dense phase catalyst zone disposed within a regenerator. A gas can be introduced to a lower zone of the dense phase catalyst zone. At least a portion of the carbon deposited on the coked catalyst particles can be combusted to provide a flue gas, heat, and a regenerated catalyst.

    摘要翻译: 提供了用于再生废催化剂的系统和方法。 该方法可以包括在催化剂颗粒存在下加热烃和焦炭前体以提供裂化的烃产物和焦化的催化剂颗粒。 裂化的烃产物和焦化的催化剂颗粒可以选择性分离以提供烃产物和焦化的催化剂颗粒。 焦化的催化剂颗粒可与载体流体混合以提供混合物。 可以将混合物引入设置在再生器内的致密相催化剂区的上表面。 可以将气体引入密相催化剂区的下部区域。 沉积在焦化催化剂颗粒上的碳的至少一部分可以燃烧以提供烟道气,热和再生催化剂。