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81.发明授权Method and device for catalytic cracking comprising in parallel at least an upflow reactor and at least a downflow reactor 有权用于催化裂化的方法和装置，其至少包括上流式反应器和至少一个下流式反应器公开(公告)号：US07220351B1
公开(公告)日：2007-05-22
申请号：US10149597
申请日：2000-11-28
摘要： An apparatus and a process for catalytic cracking of a hydrocarbon feed is described, carried out in at least two reaction zones, one (30) operating in catalyst riser mode, wherein the feed and catalyst from regeneration zone (3) are circulated from bottom to top, the first gases produced are separated from the coked catalyst in a first separation zone (38), the catalyst is stripped (40), a first cracking and stripping effluent (42) is recovered and the coked catalyst is recycled (45) to the regeneration zone. Catalyst (12) from regeneration zone (3) and a hydrocarbon feed (19) are introduced into the upper portion of a dropper reaction zone (16), the catalyst and feed being circulated from top to bottom, the coked catalyst is separated from the second gases produced in a second separation zone (20), the second gases (24) produced are recovered and the coked catalyst is recycled (25) to the regeneration zone.
摘要翻译： 描述了在至少两个反应区域中进行的用于烃进料的催化裂化的装置和方法，一个（30）以催化剂提升管模式操作，其中来自再生区（3）的进料和催化剂从底部循环到 在第一分离区（38）中将所产生的第一种气体与焦炭催化剂分离，将催化剂汽提（40），回收第一裂解和汽提流出物（42），将焦化的催化剂再循环（45）至 再生区域。 来自再生区（3）的催化剂（12）和烃进料（19）被引入滴管反应区（16）的上部，催化剂和进料从顶部向底部循环，将焦化的催化剂从 在第二分离区（20）中产生的第二气体，回收所生产的第二气体（24），并将焦化的催化剂再循环（25）至再生区。
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82.发明申请公开(公告)号：US20050261531A1
公开(公告)日：2005-11-24
申请号：US10851486
申请日：2004-05-21
申请人： Richard Stell , George Balinsky , James McCoy , Paul Keusenkothen
发明人： Richard Stell , George Balinsky , James McCoy , Paul Keusenkothen
摘要： A process for cracking hydrocarbon feedstock containing resid comprising: heating the feedstock, mixing the heated feedstock with a fluid and/or a primary dilution steam stream to form a mixture, flashing the mixture to form a vapor phase and a liquid phase which collect as bottoms and removing the liquid phase, separating and cracking the vapor phase, and cooling the product effluent, wherein the bottoms are maintained under conditions to effect at least partial visbreaking. The visbroken bottoms may be steam stripped to recover the visbroken molecules while avoiding entrainment of the bottoms liquid. An apparatus for carrying out the process is also provided.
摘要翻译： 一种用于裂化含有渣油的烃原料的方法，包括：加热原料，将加热的原料与流体和/或初级稀释蒸汽流混合以形成混合物，使混合物闪蒸形成气相和液相， 并除去液相，分离和裂化气相，以及冷却产物流出物，其中底部保持在至少部分减粘裂化的条件下。 脱硫塔底物可以蒸汽汽提以回收分解的分子，同时避免夹带底部液体。 还提供了一种用于执行该过程的装置。
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公开(公告)号：US20030062291A1
公开(公告)日：2003-04-03
申请号：US10127930
申请日：2002-04-23
IPC分类号： C10G011/00 , C10G011/02 , C10G011/04
CPC分类号： C10G51/06 , B01J29/40 , B01J2229/16 , B01J2229/36 , C07C4/06 , C09K2019/546 , C10G11/05 , C10G2400/20 , C07C11/02
摘要： A process for cracking an olefin-containing hydrocarbon feedstock which is selective towards light olefins in the effluent, the process comprising passing a hydrocarbon feedstock containing one or more olefins through a reactor containing a crystalline silicate selected from an MFI-type crystalline silicate having a silicon/aluminium atomic ratio of at least 180 and an MEL-type crystalline silicate having a silicon/aluminium atomic ratio of from 150 to 800 which has been subjected to a steaming step, at an inlet temperature of from 500 to 600null C., at an olefin partial pressure of from 0.1 to 2 bars and the feedstock being passed over the catalyst at an LHSV of from 5 to 30hnull1 to produce an effluent with an olefin content of lower molecular weight than that of the feedstock, wherein the olefin-containing hydrocarbon feedstock includes a C5-containing overhead cut from a first fractionator which has been fed with a C5null hydrocarbon feedstock, the-bottom fraction from the first fractionator being a C6null cut and the C5null hydrocarbon feedstock comprises a bottom fraction from a second fractionator which has been fed with a feedstock having at least C4null hydrocarbons, and the overhead from the second fractionator comprises a C4 containing cut, optionally further containing C3 hydrocarbons.
摘要翻译： 一种用于裂解对流出物中的轻质烯烃具有选择性的含烯烃的烃原料的方法，该方法包括使含有一种或多种烯烃的烃原料通过含有选自具有硅的MFI型结晶硅酸盐的结晶硅酸盐的反应器 /铝原子比为180以上的硅/铝原子比为150〜800的MEL型结晶硅酸盐，其入口温度为500〜600℃，进行了蒸汽工序，在 烯烃分压为0.1至2巴，原料以5至30h -1的LHSV通过催化剂以产生具有比原料低的分子量的烯烃含量的流出物，其中烯烃 - 含有碳氢化合物的原料包括来自已经进料有C5 +烃原料的第一分馏塔的含C5塔顶馏分，来自第一馏分的底馏分 或者是C6 +馏分，并且C5 +烃原料包含来自第二分馏塔的底部馏分，该第二分馏器已经供给具有至少C4 +烃的原料，并且来自第二分馏塔的塔顶馏出物包含含C4馏分，任选地还含有C 3烃。
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公开(公告)号：US5516420A
公开(公告)日：1996-05-14
申请号：US240402
申请日：1994-05-10
申请人： Lee M. Henton
发明人： Lee M. Henton
摘要： Disclosed is a method for improving fluid cracking catalyst performance by increasing metal contamination incrementally while cracking two different feedstocks that have different concentrations of metal contaminants. The relative amount of metal contamination is controlled by magnetic separation. The incrementally increased cracking catalyst is used in cracking a second feedstock.
摘要翻译： 公开了一种通过增加金属污染来改善流体裂化催化剂性能的方法，同时破裂具有不同浓度金属污染物的两种不同原料。 金属污染的相对量由磁力分离控制。 逐渐增加的裂化催化剂用于裂化第二原料。
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85.发明授权Process for catalytically cracking feedstocks paraffin rich comprising high and low concarbon components 失效用于催化裂化原料的方法富含石蜡和高碳组分的石蜡
公开(公告)号：US5435906A
公开(公告)日：1995-07-25
申请号：US104178
申请日：1993-08-09
申请人： Axel R. Johnson , Joseph L. Ross , Atulya V. Saraf
发明人： Axel R. Johnson , Joseph L. Ross , Atulya V. Saraf
摘要： A process for contemporaneously catalytically cracking a paraffin rich feedstock and a heavy feedstock wherein the feedstocks are segregated prior to catalytic cracking in separate reactors with regenerated particulate catalyst solids. The process provides for the separate optimal cracking of paraffinic constituents and heavy naphthenic constituents while maintaining an overall heat balance.
摘要翻译： 同时催化裂化含石蜡原料和重质原料的方法，其中原料在具有再生颗粒催化剂固体的分离的反应器中在催化裂化之前被分离。 该方法提供了链烷烃组分和重质环烷烃组分的单独的最佳裂化，同时保持总体热平衡。
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公开(公告)号：US5009769A
公开(公告)日：1991-04-23
申请号：US496164
申请日：1990-03-19
申请人： Alan R. Goelzer
发明人： Alan R. Goelzer
摘要： An improved process and apparatus is provided for simultaneously, independently catalytically cracking dissimilar hydrocarbon feedstocks at elevated temperatures in separate riser reactors and under respective operating parameters which permit selective conversion to desired products, wherein catalyst regeneration is conducted in two steps comprising separate relatively lower and higher temperature regeneration stages.
摘要翻译： 提供了一种改进的方法和装置，用于在分离的提升管反应器中和在允许选择性转化成所需产物的相应操作参数下同时，独立地在不同的烃原料上催化裂解不同的烃原料，其中催化剂再生在两个步骤中进行，包括分开的相对较低和较高 温度再生阶段。
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公开(公告)号：US4428823A
公开(公告)日：1984-01-31
申请号：US455355
申请日：1983-01-03
CPC分类号： C10G51/06
摘要： An integrated hydrocarbon conversion process wherein two different heavy oil feed streams are thermally processed is disclosed. Preferably a vacuum gas oil is charged to a thermal cracking zone and a reduced crude fraction is charged to a visbreaking heater. The effluent of each thermal operation is separated into vapor and liquid fractions, with the vapor fractions being fed to a product fractionator. The liquid fractions each enter separate but interconnected subatmospheric pressure separation zones, one of which is a vacuum column. The bottoms of a product fractionator and distillate from the vacuum column are also charged to the thermal cracking zone.
摘要翻译： 公开了一种其中热处理两种不同重油进料流的综合烃转化方法。 优选将真空瓦斯油装入热裂解区，将还原的粗馏分装入减粘裂化加热器。 每个热操作的流出物被分离成蒸气和液体馏分，蒸气馏分被供给到产物分馏器。 液体馏分各自进入分离但相互连接的低于大气压的压力分离区，其中一个是真空塔。 来自真空塔的产物分馏塔和馏出物的塔底物也被装入热裂解区。
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公开(公告)号：US4265731A
公开(公告)日：1981-05-05
申请号：US110304
申请日：1980-01-08
申请人： Norris W. Mitchell
发明人： Norris W. Mitchell
摘要： A method and apparatus for separating a residual crude oil into a light oil fraction and a heavy oil fraction in which the oil is first separated into a first light oil fraction and a first heavy oil fraction, the first heavy oil fraction is further separated into a second light oil fraction, an intermediate oil fraction and a second heavy oil fraction and the intermediate fraction is recycled to the first separation step.
摘要翻译： 将残留原油分离成轻油馏分和重质油馏分的方法和装置，其中油首先分离成第一轻油馏分和第一重油馏分，将第一重油馏分进一步分离成 第二轻油馏分，中间油馏分和第二重油馏分，并将中间馏分再循环至第一分离步骤。
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89.发明授权Integrated fractionation, fluid coking and catalytic cracking process for hydrocarbon oils 失效烃油的综合分馏，流体焦化和催化裂化过程
公开(公告)号：US2852439A
公开(公告)日：1958-09-16
申请号：US38297753
申请日：1953-09-29
发明人： JAHNIG CHARLES E , BARR FRANK T , BROWN JAMES W
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公开(公告)号：US2526068A
公开(公告)日：1950-10-17
申请号：US75224747
申请日：1947-06-03
发明人： JEAN DELATTRE-SEGUY
IPC分类号： C10G51/06
CPC分类号： C10G51/06
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