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    Process for fluid catalytic cracking of hydrocarbon feedstocks with high levels of basic nitrogen
    1.
    发明申请
    Process for fluid catalytic cracking of hydrocarbon feedstocks with high levels of basic nitrogen 审中-公开
    具有高水平碱性氮的烃原料的流化催化裂化方法

    公开(公告)号：US20060283777A1

    公开(公告)日：2006-12-21

    申请号：US11513020

    申请日：2006-08-31

    申请人： Claudia Maria de Alvarenga Baptista ,  Elizabeth Moreira ,  Henrique Cerqueira

    发明人： Claudia Maria de Alvarenga Baptista ,  Elizabeth Moreira ,  Henrique Cerqueira

    IPC分类号： C10G11/00

    CPC分类号： C10G11/18 ,  C10G11/05 ,  C10G11/187

    摘要： A process is described for fluid catalytic cracking of hydrocarbons with high levels of basic nitrogen, where hydrocarbon feedstocks A and B with different levels of basic nitrogen are injected in a segregated fashion, into different risers of a multiple riser FCCU that possesses at least two risers. The injection of the feedstocks is made in such a way that feedstock A, to be injected in the riser with greater volume—main riser 7—possessing a level of basic nitrogen at least 200 ppm lower than the level of feedstock B to be injected into the riser with lower volume—secondary riser (8).

    摘要翻译： 描述了一种用于具有高水平碱性氮的烃的流体催化裂解的方法，其中具有不同水平的碱性氮的烃原料A和B以分离的方式注入到具有至少两个提升管的多提升管FCCU的不同提升管中 。 原料的注入以这样一种方式进行，使原料A注入提升管中较大体积主提升管7，其具有比待注入的原料B的水平低至少200ppm的碱性氮的水平 具有较低容积的二次提升管（8）的立管。

    Process and device to optimize the yield of fluid catalytic cracking products
    3.
    发明申请
    Process and device to optimize the yield of fluid catalytic cracking products 有权
    流化床装置优化流化床催化裂化产物的产率

    公开(公告)号：US20060021909A1

    公开(公告)日：2006-02-02

    申请号：US11190863

    申请日：2005-07-28

    申请人： Henrique Cerqueira ,  Claudia Alvarenga Baptista ,  Willam Gilbert ,  Oscar Pravia

    发明人： Henrique Cerqueira ,  Claudia Alvarenga Baptista ,  Willam Gilbert ,  Oscar Pravia

    IPC分类号： C10G11/00 ,  B01J8/18

    CPC分类号： B01J8/0055 ,  B01J8/1818 ,  B01J8/1872 ,  B01J2208/00707 ,  C10G11/182

    摘要： A process and device to optimize the yield of fluid catalytic cracking products through a reactive stripping process are disclosed. One or more hydrocarbon streams (3) are introduced in an intermediary region of the stripper (1) of a fluid catalytic cracking unit (FCC), from a device that allows a homogeneous distribution with adequate dispersion. This/these stream(s) react(s) with the catalyst of FCC, although its activity is reduced due to the adsorption of hydrocarbons in the reaction zone, generating products that improve and/or change the global distribution of products, providing a refinery profile adequate to meet quality demands and requirements.

    摘要翻译： 公开了通过反应性汽提过程来优化流化催化裂化产物的产率的方法和装置。 一种或多种烃流（3）从允许均匀分布且具有适当分散体的装置引入流化催化裂化装置（FCC）的汽提器（1）的中间区域。 这些/这些流与FCC的催化剂反应，尽管其活性由于在反应区中的烃的吸附而减少，产生改善和/或改变产品的全球分布的产品，提供炼油厂 外形足以满足质量要求和要求。

    Stripping apparatus and process
    4.
    发明申请
    Stripping apparatus and process 失效
    剥皮装置和工艺

    公开(公告)号：US20050040075A1

    公开(公告)日：2005-02-24

    申请号：US10643968

    申请日：2003-08-20

    申请人： Henrique Cerqueira ,  Claudia M Alvarenga Baptista ,  Jose Fusco

    发明人： Henrique Cerqueira ,  Claudia M Alvarenga Baptista ,  Jose Fusco

    IPC分类号： B01D45/08 ,  B01J8/00 ,  B01J8/18 ,  C10G11/00 ,  C10G11/05 ,  C10G11/18

    CPC分类号： B01D45/08 ,  B01J8/18 ,  C10G11/05 ,  C10G11/182

    摘要： A stripping apparatus for desorbing gases from solid particles through which flows counter-currently a stripping fluid is described, which comprises a series of sets of at least two parallel, segmented, baffle plates each, with the segmented baffles being oriented so that the rows are offset relative to rows of other levels, where the thickness and separation of said sets of baffles is so dimensioned as to reduce coalescence of the size of the formed bubbles and optimize the hydrocarbons desorption from said fluidized solid particles. The solid particles are mainly spent catalyst particles from a FCC process. The stripping process to be carried out in a fluidized bed comprises contacting the spent catalyst with a stripping fluid that flows upwardly in the fluidized bed in the form of bubbles. Adsorbed hydrocarbons present in the spent catalyst are transferred from the catalyst emulsion that flows downwardly to the upwardly moving bubbles, so as to promote the efficient recovery of cracked products.

    摘要翻译： 描述了一种用于从固体颗粒解吸气体的汽提装置，通过该汽提装置反向流动汽提流体，其包括一系列至少两个平行的，分段的挡板，每个分段挡板被定向成使得行是 相对于其他级别的行偏移，其中所述挡板组的厚度和分离的尺寸被设计成减小形成的气泡的尺寸的聚结并优化烃从所述流化固体颗粒的解吸附。 固体颗粒主要是来自FCC工艺的废催化剂颗粒。 在流化床中进行的汽提过程包括使废催化剂与气泡形式的流化床中向上流动的汽提流体接触。 存在于废催化剂中的吸附烃从向下流动的催化剂乳液转移到向上移动的气泡，以促进裂化产物的有效回收。

    Process for the fluid catalytic cracking of mixed feedstocks of hydrocarbons from different sources
    6.
    发明申请
    Process for the fluid catalytic cracking of mixed feedstocks of hydrocarbons from different sources 有权
    来自不同来源的烃混合原料流化催化裂化的方法

    公开(公告)号：US20060163116A1

    公开(公告)日：2006-07-27

    申请号：US10559528

    申请日：2004-05-19

    申请人： Claudia Maria de Lacerda Baptista ,  Henrique Cerqueira ,  Emanuel Sandes

    发明人： Claudia Maria de Lacerda Baptista ,  Henrique Cerqueira ,  Emanuel Sandes

    IPC分类号： C10G11/04

    CPC分类号： C10G11/18 ,  C10G2400/28

    摘要： A process for the fluid catalytic cracking of mixed hydrocarbon feeds from different sources is described, such as feeds A and B of different crackability, the process being especially directed to obtaining light fractions such as LPG and comprising injecting feed A in the base of the riser reactive section and feed B, of lower crackability, at a height between 10% and 80% of the riser, with feed B comprising between 5% and 50% of the total processed feed. The process requires that the feeds present differences in the contaminant content, improved dispersion of feeds A and B and feed B injection temperature same or higher than that of feed A.

    摘要翻译： 描述了用于来自不同来源的混合烃进料的流化催化裂化的方法，例如不同裂化性的进料A和B，该方法特别涉及获得轻馏分如LPG，并且包括将提取物A的基料中注入进料A 反应段和进料B在提升管的10％至80％之间的高度处具有较低的可裂性，进料B占加工进料总量的5％至50％。 该方法要求进料存在污染物含量的差异，改善进料A和B的分散性，并将B进料温度与进料A相同或更高。