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公开(公告)号：US07435335B1
公开(公告)日：2008-10-14
申请号：US09553107
申请日：2000-04-20
CPC分类号： C10G65/12
摘要： A process for hydroprocessing a distillate stream to produce a stream exceptionally low in sulfur, with total aromatics and polynuclear aromatics being moderately reduced. A distillate stream is hydrodesulfurized in a first hydrodesulfurization stage. The product stream thereof is passed to a first separation stage wherein a vapor phase product stream and a liquid product stream are produced. The liquid phase product stream is passed to a second hydrodesulfurization stage and the product stream thereof is passed to a second separation stage wherein a vapor phase product stream and a liquid product stream low in sulfur are produced. At least a portion of the vapor product stream from said second separation stage can be cascaded to the first hydrodesulfurization stage.
摘要翻译： 用于加氢处理馏出物流以产生异常低硫的流的方法，其中芳族化合物和多环芳烃被适度地还原。 馏出物流在第一加氢脱硫阶段加氢脱硫。 其产物流被送到第一分离阶段，其中产生气相产物流和液体产物流。 将液相产物流送至第二加氢脱硫阶段，将其产物流送至第二分离阶段，其中产生气相产物流和硫含量低的液体产物流。 来自所述第二分离级的至少一部分蒸汽产物流可以级联到第一加氢脱硫阶段。
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公开(公告)号：US06824673B1
公开(公告)日：2004-11-30
申请号：US09553374
申请日：2000-04-20
申请人： Edward S. Ellis , Henry Jung , William E. Lewis , Larry L. Iaccino , Michele S. Touvelle , Gordon F. Stuntz
发明人： Edward S. Ellis , Henry Jung , William E. Lewis , Larry L. Iaccino , Michele S. Touvelle , Gordon F. Stuntz
IPC分类号： C10G4500
CPC分类号： C10G65/12
摘要： A process for producing distillate boiling range streams that are low in both sulfur and aromatics. A distillate feedstock is treated in a first hydrodesulfurization stage in the presence of a hydrogen-containing treat gas and a hydrodesulfurization catalyst, thereby resulting in partial desufurization of the stream. The partially desulfurized distillate stream is then treated in a second hydrodesulfurization stage, also in the presence of a hydrogen-containing treat gas and a hydrodesulfurization catalyst. The hydrogen-containing treat gas is cascaded from the next downstream reaction stage, which is an aromatics hydrogenation stage.
摘要翻译： 一种生产硫和芳烃含量低的馏出物沸腾物流的方法。 在含氢处理气体和加氢脱硫催化剂的存在下，在第一加氢脱硫阶段处理馏出物原料，从而导致料流的部分脱硫。 然后在第二加氢脱硫阶段，在含氢处理气体和加氢脱硫催化剂的存在下处理部分脱硫的馏出物物流。 含氢处理气体从下一个下游反应阶段级联，其是芳族化合物氢化反应阶段。
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公开(公告)号：US06893475B1
公开(公告)日：2005-05-17
申请号：US09553108
申请日：2000-04-20
申请人： Edward S. Ellis , Lynne Gillespie , Michele S. Touvelle , William E. Lewis , Gordon F. Stuntz , Lisa I. Yeh
发明人： Edward S. Ellis , Lynne Gillespie , Michele S. Touvelle , William E. Lewis , Gordon F. Stuntz , Lisa I. Yeh
CPC分类号： C10G65/12
摘要： A distillate fuel composition boiling in the range of about 190° C. to 400° C. with a T10 point greater than 205° C., and having a sulfur level of less than about 100 wppm, a total aromatics content of about 15 to 35 wt. %, a polynuclear aromatics content of less than about 3 wt. %, wherein the ratio of total aromatics to polynuclear aromatics is greater than about 11.
摘要翻译： 馏出物燃料组合物在约190℃至400℃的范围内沸腾，T10点大于205℃，硫含量低于约100wppm，总芳烃含量为约15至 35重量％ ％，多核芳烃含量小于约3wt。 ％，其中总芳族化合物与多环芳族化合物的比例大于约11。
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公开(公告)号：US06837989B2
公开(公告)日：2005-01-04
申请号：US10264445
申请日：2002-10-02
申请人： Gordon F. Stuntz , George A. Swan, III , William E. Winter , Michel Daage , Michele S. Touvelle , Darryl P. Klein
发明人： Gordon F. Stuntz , George A. Swan, III , William E. Winter , Michel Daage , Michele S. Touvelle , Darryl P. Klein
CPC分类号： C10G69/04
摘要： The invention relates to a process for converting cycle oils produced in catalytic cracking reactions into olefin and naphtha. More particularly, the invention relates to a process for hydroprocessing a catalytically cracked light cycle oil, and then re-cracking it in an upstream zone of the primary FCC riser reactor.
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公开(公告)号：US06811682B2
公开(公告)日：2004-11-02
申请号：US10264449
申请日：2002-10-02
申请人： Gordon F. Stuntz , George A. Swan, III , William E. Winter , Michel Daage , Michele S. Touvelle , Darryl P. Klein
发明人： Gordon F. Stuntz , George A. Swan, III , William E. Winter , Michel Daage , Michele S. Touvelle , Darryl P. Klein
IPC分类号： C10G5102
CPC分类号： C10G69/04
摘要： The invention relates to a process for converting cycle oils produced in catalytic cracking reactions into light olefin and naphtha. More particularly, the invention relates to a process for hydroprocessing a catalytically cracked light cycle oil in order to form a hydroprocessed cycle oil containing a significant amount of tetralins. The hydroprocessed cycle oil is then re-cracked in an upstream zone of the primary FCC riser reactor.
摘要翻译： 本发明涉及将在催化裂化反应中生产的循环油转化成轻质烯烃和石脑油的方法。 更具体地，本发明涉及用于加氢处理催化裂化的轻循环油的方法，以形成含有大量四氢化萘的加氢循环油。 然后，加氢循环油在初级FCC提升管反应器的上游区域再裂化。
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6.发明申请DRYING DEVICE FOR PRODUCING SMALL QUANTITIES OF CONTROLLED PARTICLE SIZE CATALYSTS WHICH ARE APPROPRIATE FOR USE IN FLUIDIZED BED OPERATIONS SUCH AS FLUID CATALYTIC CRACKING 审中-公开用于生产适用于流化床操作的受控粒度催化剂的小量数量的干燥装置，如流体催化裂化公开(公告)号：US20110152062A1
公开(公告)日：2011-06-23
申请号：US12957817
申请日：2010-12-01
申请人： William A. Wachter , Brenda A. Raich , Theodore E. Datz , David O. Marler , Nicholas Rollman , Jeffrey T. Elks , Gordon F. Stuntz
发明人： William A. Wachter , Brenda A. Raich , Theodore E. Datz , David O. Marler , Nicholas Rollman , Jeffrey T. Elks , Gordon F. Stuntz
CPC分类号： B01J29/06 , B01J29/70 , B01J37/0018 , B01J37/0072 , B01J37/0236 , B01J37/08 , B01J2229/36 , B01J2229/42 , C10G11/05
摘要： Catalysts for experimentation are produced having a controlled matrix pore structure. The manufacturing process utilizes tape casting in the drying procedure in which a catalyst slurry is cast on a substrate and dried at a temperature of between about 50° C. to 200° C. for a period of time of about 0.1 to 1.0 hour. The dried catalyst particles can be removed from the substrate by several techniques, including scraping, burning, and deforming the substrate material, The resulting catalytic particles can be produced in an amount of about ca. 3 g to 300 g from slurries with volumes between 5 cc to 500 cc, which are suitable for small scale FCC reactors and for high throughput experimentation.
摘要翻译： 生产具有受控矩阵孔结构的用于实验的催化剂。 制造方法在干燥过程中使用带铸造，其中将催化剂浆料浇铸在基材上并在约50℃至200℃的温度下干燥约0.1至1.0小时的时间。 干燥的催化剂颗粒可以通过几种技术从基材中除去，包括刮擦，燃烧和使基材变形。所得到的催化剂颗粒可以以约约 3克至300克，体积在5毫升至500毫升之间的浆料，适用于小规模的FCC反应器和高通量实验。
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7.发明授权Process for selectively producing propylene in a fluid catalytic cracking process 失效在流化催化裂化过程中选择性生产丙烯的方法公开(公告)号：US06803494B1
公开(公告)日：2004-10-12
申请号：US09574261
申请日：2000-05-19
申请人： Paul K. Ladwig , John E. Asplin , Gordon F. Stuntz , William A. Wachter , Brian Erik Henry , Shun C. Fung
发明人： Paul K. Ladwig , John E. Asplin , Gordon F. Stuntz , William A. Wachter , Brian Erik Henry , Shun C. Fung
IPC分类号： C07C406
CPC分类号： C10G51/023 , C10G11/18 , C10G51/026 , C10G57/02 , C10G2400/20
摘要： A process for producing polypropylene from olefins selectively produced from a catalytically cracked or thermally cracked naphtha stream is disclosed herein. The naphtha stream is contacted with a catalyst containing from about 10 to 50 wt. % of a crystalline zeolite having an average pore diameter less than about 0.7 nanometers at reaction conditions which include temperatures from about 500° C. to 650° C. and a hydrocarbon partial pressure from about 10 to 40 psia. The catalyst may be pre-coked with a carbonaceous feed. Alternatively, the carbonaceous feed used to coke the catalyst may be co-fed with the naphtha feed.
摘要翻译： 本文公开了从催化裂化或热裂化石脑油流选择性地生产的烯烃生产聚丙烯的方法。 将石脑油流与含有约10至50wt。 在包括约500℃至650℃的温度和约10至40psia的烃分压的反应条件下，平均孔径小于约0.7纳米的结晶沸石的％。 催化剂可以用碳质进料预结焦。 或者，用于焦化催化剂的碳质原料可以与石脑油进料共同进料。
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8.发明授权Naphtha cracking and hydroprocessing process for low emissions, high octane fuels 失效用于低排放，高辛烷值燃料的石脑油裂解和加氢处理方法公开(公告)号：US06315890B1
公开(公告)日：2001-11-13
申请号：US09436660
申请日：1999-11-10
IPC分类号： C10G6904
CPC分类号： C10G51/023 , C10G57/02 , C10G69/04 , C10G69/06 , C10G2400/20
摘要： The invention is related to a two step process wherein the first step comprises cracking an olefinic naphtha resulting in a cracked product having a diminished total concentration of olefinic species. The second step comprises hydroprocessing at least a portion of the cracked product, especially a naphtha fraction, to provide a hydroprocessed cracked product having a reduced concentration of contaminant species but without a substantial octane reduction.
摘要翻译： 本发明涉及两步法，其中第一步骤包括裂化烯烃石脑油，产生具有减少的烯属物质总浓度的裂化产物。 第二步骤包括对至少一部分裂化产物，特别是石脑油馏分进行加氢处理，以提供具有降低的污染物质浓度但没有显着辛烷值降低的加氢裂化产物。
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公开(公告)号：US5320746A
公开(公告)日：1994-06-14
申请号：US608130
申请日：1990-11-01
摘要： A process for recovering oil from tar sands by subjecting the tar sands to aqueous extraction to produce a bitumen-rich layer containing bitumen, water and solids and a bitumen-lean layer containing relatively less bitumen and relatively more water and solids. The solids present in the bitumen-lean layer contain a substantial portion of finely divided clay having adhered organic matter. The clay solids are retained with the bitumen from the bitumen-lean layer and the bitumen-clay mixture is pyrolyzed. Pyrolysis of the bitumen-lean layer containing clay having adhered organic matter reduces the volume of aqueous tailings which would otherwise be produced and also results in increased hydrocarbon yields.
摘要翻译： 通过对焦油砂进行含水萃取以产生含有沥青，水和固体的沥青富含层以及含有相对较少的沥青和相对较多的水和固体的沥青贫层，从沥青砂中回收油的方法。 存在于贫沥青层中的固体含有大部分具有粘附有机物质的细碎粘土。 粘土固体与贫沥青层的沥青一起保留，沥青 - 粘土混合物被热解。 含有附着有机物质的含有粘土的贫沥青层的热解减少了否则将产生的含水尾矿的体积，并且还导致增加的烃产率。
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公开(公告)号：US4504380A
公开(公告)日：1985-03-12
申请号：US525826
申请日：1983-08-23
申请人： Gordon F. Stuntz , Terry A. Reid
发明人： Gordon F. Stuntz , Terry A. Reid
CPC分类号： C10G11/04 , C10G11/18 , Y10S502/521
摘要： A method for passivating metal contaminants present in a hydrocarbon feedstock which become deposited on cracking catalyst is described. The method is directed at passing the cracking catalyst through a passivation zone having a reducing atmosphere maintained at an elevated temperature by the introduction of a process reducing gas. The unsaturated hydrocarbon content of the reducing gas is decreased prior to the introduction of the process reducing gas into the passivation zone to thereby lower the rate of coke formation. In a preferred embodiment process reducing gas is passed through a hydrogenation zone adapted to hydrogenate an unsaturated hydrocarbon present in the process reducing gas prior to the process reducing gas being added to the passivation zone.
摘要翻译： 描述了一种钝化沉积在裂化催化剂上的烃原料中存在的金属污染物的方法。 该方法涉及通过引入工艺还原气体使裂化催化剂通过具有保持在高温下的还原气氛的钝化区。 在将工艺还原气体引入钝化区之前，还原气体的不饱和烃含量降低，从而降低焦炭形成速率。 在一个优选的实施方案中，还原气体通过适于在工艺中存在的不饱和烃氢化的氢化区，还原气体在还原气体被加入钝化区之前。
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