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1.发明授权
公开(公告)号：US4818372A
公开(公告)日：1989-04-04
申请号：US111115
申请日：1987-10-20
CPC分类号： C10G11/187 , C10G11/18 , Y10S208/01
摘要： An apparatus for the catalytic cracking of hydrocarbon feedstocks with reaction temperature control is provided which includes an upward-flow or downward-flow cracking column, means for feeding said column under pressure with a hydrocarbon feedstock and with particles of a regenerated cracking catalyst, at least one means for injection of an auxiliary fluid downstream of the zone in said column where the hydrocarbon feedstock and the regenerated catalyst particles are contacted with each other, to reduce the temperature of the reaction zone situated directly downstream thereof, means for separating the products of the cracked feedstock and the spent catalyst particles, at least one stripping means, at least one unit for regeneration of the catalyst by combustion of the coke deposited thereon and means for recycling the regenerated catalyst to said feeding means.
摘要翻译： 提供了一种用于反应温度控制的烃原料的催化裂化装置，其包括向上流动或向下流动裂化塔，用于在压力下用烃原料和再生裂化催化剂颗粒供给所述塔的装置，至少 一种用于将烃原料和再生催化剂颗粒彼此接触的在所述塔中的区域下游注入辅助流体的方法，以降低位于其下游的反应区域的温度，用于分离产物的装置 裂化原料和废催化剂颗粒，至少一个汽提装置，至少一个用于通过燃烧沉积在其上的焦炭催化剂再生的单元和用于将再生催化剂再循环到所述进料装置的装置。
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公开(公告)号：US4795548A
公开(公告)日：1989-01-03
申请号：US923190
申请日：1986-10-27
摘要： A process for the production of anode grade coke from a hydrocarbon feed characterized by high levels of sulfur and metals comprises subjecting a vacuum resid to a fluidized bed coking process so as to produce gas, distillates, coke and a residual bottom stream, filtering the residual stream so as to remove solids and thereafter coking the filtered stream.
摘要翻译： 由烃类进料生产阳极级焦炭的方法，其特征在于高含量的硫和金属包括将真空渣油经受流化床焦化过程，以产生气体，馏出物，焦炭和残余底部流，过滤残留物 流以除去固体，然后焦化过滤的流。
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公开(公告)号：US4234411A
公开(公告)日：1980-11-18
申请号：US20771
申请日：1979-03-15
申请人： Gregory J. Thompson
发明人： Gregory J. Thompson
CPC分类号： C10G11/187 , Y10S208/01
摘要： An improved fluid catalytic cracking process providing improved product yield and selectivity which employs a split flow of recycled, regenerated catalyst to the reactor riser. Process operating temperatures control the flow rates of the recycled, regeneration catalyst.
摘要翻译： 改进的流化催化裂化方法提供改进的产物产率和选择性，其使用再循环的再生催化剂的分流流向反应器提升管。 工艺操作温度控制循环再生催化剂的流速。
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公开(公告)号：US4178228A
公开(公告)日：1979-12-11
申请号：US913307
申请日：1978-06-07
申请人： Bong H. Chang
发明人： Bong H. Chang
CPC分类号： C10G51/023 , C10G9/00
摘要： A mild thermal cracking of gas oil in the presence of added olefinic naphtha increases the yield of middle distillate.
摘要翻译： 在加入的烯烃石脑油的情况下，瓦斯油的轻度热裂解可提高中间馏分的产率。
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5.发明授权Conversion of asphaltene-containing charge stocks and product separation process 失效含沥青质的电荷原料转化和产物分离过程
公开(公告)号：US4124486A
公开(公告)日：1978-11-07
申请号：US833331
申请日：1977-09-14
申请人： John P. Nolley, Jr.
发明人： John P. Nolley, Jr.
CPC分类号： C10G49/22 , B01D11/0407 , C10G2300/107
摘要： A mixture of a hydrocarbon-selective solvent -- e.g. isobutane -- and deasphalted oil is separated in a two-stage hot-separator system at progressively higher temperatures and substantially the same pressure. Resulting vaporous phases are subjected to a cold-flash separation at a lower pressure and a considerably lower temperature. The initial hot separation, in the two-stage system, is effected at a temperature from about 1.0.degree. F. to about 25.degree. F. above the critical temperature of the solvent; the second is conducted at a temperature about 30.degree. F. to about 130.degree. F. above that in the initial hot-separation. This technique is especially advantageous when integrated into a catalytic slurry process for the conversion of metal- and asphaltene-containing hydrocarbonaceous black oils.
摘要翻译： 烃选择性溶剂的混合物。 异丁烷和脱沥青油在逐步升高的温度和基本相同的压力下在两级热分离器系统中分离。 所得气相在较低压力和相当低的温度下进行冷闪分离。 在两级系统中的初始热分离在高于溶剂的临界温度约1.0°F至约25°F的温度下进行; 第二次在初始热分离中温度约30°F至约130°F的温度下进行。 当整合到用于转化含金属和含沥青质的含烃黑油的催化淤浆法时，该技术是特别有利的。
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6.发明授权Method and system for effecting catalytic cracking of high boiling hydrocarbons with fluid conversion catalysts 失效用流体转化催化剂进行高沸点烃的催化裂化的方法和系统
公开(公告)号：US4116814A
公开(公告)日：1978-09-26
申请号：US816849
申请日：1977-07-18
申请人： John C. Zahner
发明人： John C. Zahner
CPC分类号： B01J8/26 , C10G11/18 , C10G11/182 , C10G51/06 , Y10S423/16
摘要： A method and system for cracking hydrocarbons with distinct fluid catalyst particles differing in activity, selectivity and physical characteristics is described wherein a common catalyst regeneration system is employed which will measurably contribute to the heat requirements of the operation as well as the activity/selectivity characteristics of the catalyst employed. Except for size, the catalysts upon make-up may have different or identical catalytic characteristics. However, upon contact with a particular hydrocarbon stream, such as vacuum resid, the selectivity and coke producing characteristics of the catalysts may be altered.
摘要翻译： 描述了用活性，选择性和物理特性不同的不同流体催化剂颗粒裂解烃的方法和系统，其中使用通常的催化剂再生系统，其可测量地有助于操作的热需求以及活性/选择性特性 所用的催化剂。 除了大小，化妆品上的催化剂可能具有不同或相同的催化特性。 然而，当与特定烃流（例如真空渣油）接触时，可改变催化剂的选择性和焦炭产生特性。
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公开(公告)号：US4100218A
公开(公告)日：1978-07-11
申请号：US801713
申请日：1977-05-31
申请人： Nai Yuen Chen , Werner O. Haag
发明人： Nai Yuen Chen , Werner O. Haag
CPC分类号： C07C15/00 , C07C2/00 , C07C4/04 , C07C9/02 , C07C2529/06 , C10G2400/30
摘要： Ethane is converted to LPG and gasoline and/or aromatics concentrate in a combination process which comprises directly passing olefin effluent from the thermal cracking of ethane over a special crystalline aluminosilicate zeolite of the ZSM-5 type and recovering aromatics and C.sub.3 + hydrocarbons. For best yields, the thermal cracking step is conducted under more severe conditions than are used when ethylene production is optimized. The second, olefin conversion step is carried out at either the same pressure as the cracking step or higher. The process is of particular interest where low cost ethane is available.
摘要翻译： 将乙烷转化为LPG，并将汽油和/或芳烃浓缩物转化为组合方法，其包括将乙烯热裂解的烯烃流出物直接通过ZSM-5型的特殊结晶硅铝酸盐沸石，并回收芳族化合物和C3 +烃。 为获得最佳产率，热裂解步骤在比乙烯生产优化时使用的条件更严格的条件下进行。 第二个烯烃转化步骤在与裂化步骤相同的压力下进行或更高。 在低成本乙烷可用的情况下，这个过程特别有意义。
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公开(公告)号：US4090948A
公开(公告)日：1978-05-23
申请号：US760247
申请日：1977-01-17
摘要： An improvement in the fluid cracking process is obtained by contacting the hydrocarbon feed in a riser reaction zone first with a recycled coke-containing spent catalyst and then contacting the resultant mixture with freshly regenerated catalyst to produce the desired conversion of the hydrocarbon feed and a coke-containing spent catalyst, a portion of the spent catalyst being recycled without regeneration to the inlet of the reaction zone and the remainder being regenerated and returned to an intermediate point in the reaction zone. The recycled coke-containing spent catalyst has sufficient activity so that the highly reactive nitrogen and carbon residue containing hydrocarbon contaminants in the oil feed will deposit on the spent catalyst and thus minimize the deactivation of the freshly regenerated catalyst used in the subsequent cracking of the oil feed.By contacting the oil feed first with the recycled spent catalyst, this invention allows the refiner to utilize the full activity and selectivity characteristics of the freshly regenerated catalyst in order to obtain higher yields of the desired products from the cracking operations.
摘要翻译： 通过使提质管反应区中的烃进料首先与再循环的含焦炭废催化剂接触，然后使所得混合物与新鲜再生的催化剂接触以产生烃进料和焦炭所需的转化率，从而获得流体裂解过程的改进 的废催化剂，一部分废催化剂被再循环而没有再生到反应区的入口，其余的被再生并返回到反应区中的中间点。 再循环的含焦炭废催化剂具有足够的活性，使得在油进料中含有烃类污染物的高活性氮和碳残余物将沉积在废催化剂上，从而最小化随后裂化油中所用新鲜再生催化剂的失活 饲料。
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公开(公告)号：US4067798A
公开(公告)日：1978-01-10
申请号：US661654
申请日：1976-02-26
CPC分类号： C10G35/14 , C10G2400/02
摘要： A method for catalytically cracking an isolated reactant feed, 80-100 volume percent of which is a substantially mono-aromatic hydrocarbon fraction boiling in the boiling range of heavy gasoline and the remainder of which is a vaporizable hydrocarbon fraction, under effective cracking conditions of cracking temperature, catalyst composition, catalyst activity, catalyst-to-feed weight ratio, and weight hourly space velocity, to produce an isolated product having increased low molecular weight olefin and low molecular weight mono-aromatic contents and a reduced sulfur content and having a high octane rating.
摘要翻译： 用于催化裂解分离的反应物进料的方法，其80-100体积％是在重汽油的沸程范围内沸腾的基本上单芳族烃馏分，其余部分是可汽化的烃馏分，在有效的裂解条件下开裂 温度，催化剂组成，催化剂活性，催化剂 - 进料重量比和重时空速，以产生具有增加的低分子量烯烃和低分子量单芳族含量和降低的硫含量并具有高的分离产物 辛烷值。
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公开(公告)号：US4011154A
公开(公告)日：1977-03-08
申请号：US697670
申请日：1976-06-18
CPC分类号： C10G65/00 , C10G2400/10
摘要： A process is disclosed for producing a lubricating oil base stock by: (1) fractionating a hydrocarbon feedstock boiling above 650.degree. F into a plurality of fractions including at least a lower-boiling fraction and a higher-boiling fraction; (2) contacting the lower-boiling fraction and hydrogen in a first hydrocracking zone, at hydrocracking conditions, with a hydrocracking catalyst to obtain an effluent comprising hydrocarbons boiling in the range of the feedstock and hydrocarbons boiling below the boiling range of the feedstock; (3) contacting at least the hydrocarbons boiling in the range of said feedstock formed in step (2), the higher-boiling fraction from step (1) without substantial intermediate deasphalting thereof, and hydrogen in a second hydrocracking zone, at hydrocracking conditions, with a hydrocracking catalyst to obtain a lubricating oil base stock including a plurality of lube oil fractions of reduced viscosity index spread over the range of the lube oil fractions; and recovering the lube oil base stock. Preferably, the resulting lube oil base stocks have a viscosity index spread of not more than about 15 units, preferably not more than 10, over the lube oil base stock viscosity range of light neutrals to bright stocks.
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