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1. 发明授权

US06837989B2 Cycle oil conversion process 失效
标题翻译：循环油转化过程
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
IPC分类号： C10G11/18 , C10G45/44 , C10G69/04 , C10G51/02 , C10G11/00
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.

2. 发明授权

US06811682B2 Cycle oil conversion process 失效
标题翻译：循环油转化过程
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。

3. 发明授权

US06569315B2 Cycle oil conversion process 失效
标题翻译：循环油转化过程
公开(公告)号：US06569315B2
公开(公告)日：2003-05-27
申请号：US09811168
申请日：2001-03-16
申请人： Gordon F. Stuntz , George A. Swan, III , William E. Winter
发明人： Gordon F. Stuntz , George A. Swan, III , William E. Winter
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 olefinic naphthas. More particularly, the invention relates to a process for hydroprocessing a catalytically cracked light cycle oil, and then re-cracking in an out-board FCC reactor it in order to form a naphthenic blend-stock.
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为烯烃石脑油的方法。更具体地说，本发明涉及一种加氢处理催化裂化的轻质循环油的方法，然后在外板FCC反应器中进行再裂化以形成环烷烃共混物。

4. 发明授权

US07435335B1 Production of low sulfur distillates 有权
标题翻译：生产低硫馏分
公开(公告)号：US07435335B1
公开(公告)日：2008-10-14
申请号：US09553107
申请日：2000-04-20
申请人： Edward S. Ellis , William E. Lewis , Larry L. Iaccino , Michele S. Touvelle , Gordon F. Stuntz
发明人： Edward S. Ellis , William E. Lewis , Larry L. Iaccino , Michele S. Touvelle , Gordon F. Stuntz
IPC分类号： C10G45/00 , C10G45/44
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。

5. 发明授权

US06893475B1 Low sulfur distillate fuels 有权
标题翻译：低硫馏分燃料
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
IPC分类号： C10G45/00 , C10G65/12 , C10L1/08
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。

6. 发明授权

US06824673B1 Production of low sulfur/low aromatics distillates 有权
标题翻译：生产低硫/低芳烃馏分
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。

7. 发明授权

US06258257B1 Process for producing polypropylene from C3 olefins selectively produced by a two stage fluid catalytic cracking process 失效
标题翻译：通过两阶段流化催化裂化方法选择性生产的C3烯烃生产聚丙烯的方法
公开(公告)号：US06258257B1
公开(公告)日：2001-07-10
申请号：US09517551
申请日：2000-03-02
申请人： George A. Swan, III , Michael W. Bedell , Paul K. Ladwig , John E. Asplin , Gordon F. Stuntz , William A. Wachter , B. Erik Henry
发明人： George A. Swan, III , Michael W. Bedell , Paul K. Ladwig , John E. Asplin , Gordon F. Stuntz , William A. Wachter , B. Erik Henry
IPC分类号： C10G5102
CPC分类号： C10G57/02 , C10G2400/20
摘要： A process for producing polymers from olefins selectively produced by a two stage process for selectively producing C2 to C4 olefins from a gas oil or resid is disclosed herein. The gas oil or resid is reacted in a first stage comprising a fluid catalytic cracking unit wherein it is converted in the presence of conventional large pore zeolitic catalyst to reaction products, including a naphtha boiling range stream. The naphtha boiling range stream is introduced into a second stage comprising a process unit containing a reaction zone, a stripping zone, a catalyst regeneration zone, and a fractionation zone. The naphtha feed is contacted in the reaction zone 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 ranging from about 500 to 650° C. and a hydrocarbon partial pressure from about 10 to 40 psia. Vapor products are collected overhead and the catalyst particles are passed through the stripping zone on the way to the catalyst regeneration zone. Volatiles are stripped with steam in the stripping zone and the catalyst particles are sent to the catalyst regeneration zone where coke is burned from the catalyst, which is then recycled to the reaction zone.
摘要翻译：本文公开了一种通过二级方法选择性制备聚合物的方法，用于从瓦斯油或渣油中选择性地生产C2至C4烯烃。瓦斯油或渣油在包括流化催化裂化装置的第一阶段中反应，其中在常规大孔沸石催化剂存在下将其转化为包括石脑油沸程的反应产物。将石脑油沸程流引入包含含有反应区，汽提区，催化剂再生区和分馏区的处理单元的第二阶段。石脑油进料在反应区中与含有约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具有平均孔径小于约0.7纳米的结晶沸石的百分比。蒸气产物被顶部收集，催化剂颗粒在通向催化剂再生区的途中通过汽提区。挥发物在汽提区中用蒸汽汽提，并将催化剂颗粒送入催化剂再生区，其中焦炭从催化剂燃烧，然后再循环到反应区。

8. 发明授权

US5074990A Fluid catalytic cracking using catalysts containing an alumina-on-silica component 失效
标题翻译：使用含有氧化铝 - 二氧化硅组分的催化剂进行流化催化裂化
公开(公告)号：US5074990A
公开(公告)日：1991-12-24
申请号：US543503
申请日：1990-06-25
申请人： Claude C. Culross , Gordon F. Stuntz , William E. Winter
发明人： Claude C. Culross , Gordon F. Stuntz , William E. Winter
IPC分类号： B01J21/12 , B01J29/08 , B01J37/00 , B01J37/02 , C10G11/04 , C10G11/05
CPC分类号： B01J37/0018 , B01J21/12 , B01J37/02 , C10G11/04 , C10G11/05
摘要： Disclosed is a fluid catalytic cracking process using a catalyst composite comprised of an alumina-on-silica material, an inorganic refractory oxide, and optionally a zeolite material. The alumina-on-silica material is comprised of silica particles with surface bound aluminum groups chemically bonded to the silica surface through surface oxygen atoms, which material is dispersed in a matrix of a refractory oxide.
摘要翻译：公开了使用由氧化铝 - 二氧化硅材料，无机耐火氧化物和任选的沸石材料组成的催化剂复合物的流化催化裂化方法。氧化铝 - 二氧化硅材料由具有表面结合的铝基团的二氧化硅颗粒组成，其通过表面氧原子化学键合到二氧化硅表面，该材料分散在难熔氧化物的基质中。

9. 发明授权

US5070053A FCC catalyst composition and method of making same 失效
标题翻译： FCC催化剂组合物及其制备方法
公开(公告)号：US5070053A
公开(公告)日：1991-12-03
申请号：US631561
申请日：1990-12-21
申请人： Claude C. Culross , Gordon F. Stuntz , William E. Winter, Jr.
发明人： Claude C. Culross , Gordon F. Stuntz , William E. Winter, Jr.
IPC分类号： B01J21/12 , B01J37/00 , B01J37/02 , C10G11/04 , C10G11/05
CPC分类号： C10G11/05 , B01J21/12 , B01J37/0018 , B01J37/02 , C10G11/04
摘要： Disclosed is a FCC catalyst composite, and a method of making said composite comprised of an alumina-on-silica additive, an inorganic refractory oxide, and optionally a zeolite material.
摘要翻译：公开了一种FCC催化剂复合材料，以及由氧化铝 - 二氧化硅添加剂，无机难熔氧化物和任选的沸石材料制成所述复合材料的方法。

10. 发明申请

US20110152062A1 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
标题翻译：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
IPC分类号： B01J37/08 , B01J37/10 , B01J35/10 , B01J31/06 , B01J29/04
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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