公开(公告)号：US20140024788A1

公开(公告)日：2014-01-23

申请号：US14033405

申请日：2013-09-20

Applicant: Chevron Phillips Chemical Company LP

Inventor： Robert R. McElvain ,  John D. Hottovy ,  Ralph W. Romig ,  Donald W. Verser ,  David H. Burns ,  John H. Tait ,  Richard Peacock ,  James E. Hein ,  Scott E. Kufeld ,  Carl W. Fenderson ,  Anurag Gupta ,  Dale A. Zellers

IPC: C08F2/01

CPC classification number: B01J19/0013 ,  B01J8/0015 ,  B01J19/1837 ,  B01J19/2455 ,  B01J2208/00212 ,  B01J2208/00752 ,  B01J2219/00006 ,  B01J2219/0236 ,  C08F2/01 ,  C08F6/003 ,  C08F10/00 ,  C08F110/02 ,  C08L23/00 ,  C08F2/14

Abstract: A manufacturing system for producing polyolefin includes a polymerization reactor, a flash chamber, and a purge column. In certain embodiments, the purge column may receive a solids stream directly from the flash chamber. Further, the purge column may function as a feed tank for an extruder within an extrusion/loadout system. According to certain embodiments, the manufacturing system may be configured to consume less than 445 kilowatt-hours of energy per metric ton of polyolefin produced based on consumption of electricity, steam, and fuel gas.

Abstract translation: 用于生产聚烯烃的制造系统包括聚合反应器，闪蒸室和吹扫塔。 在某些实施方案中，净化塔可以直接从闪蒸室接收固体物流。 此外，吹扫塔可用作挤出/挤出系统中的挤出机的进料罐。 根据某些实施例，制造系统可以被配置为消耗基于消耗电力，蒸汽和燃料气体的每公吨聚烯烃消耗少于445千瓦小时的能量。

公开(公告)号：US08569433B2

公开(公告)日：2013-10-29

申请号：US13656357

申请日：2012-10-19

Applicant: Chevron Phillips Chemical Company LP ,  Penny A. Zellers

Inventor： Robert R. McElvain ,  John D. Hottovy ,  Ralph W. Romig ,  Donald W. Verser ,  David H. Burns ,  John H. Tait ,  Richard Peacock ,  James E. Hein ,  Scott E. Kufeld ,  Carl W. Fenderson ,  Anurag Gupta ,  Dale A. Zellers

IPC: C08F2/00 ,  C08F4/00 ,  C08F210/00 ,  B01J10/00

CPC classification number: B01J19/0013 ,  B01J8/0015 ,  B01J19/1837 ,  B01J19/2455 ,  B01J2208/00212 ,  B01J2208/00752 ,  B01J2219/00006 ,  B01J2219/0236 ,  C08F2/01 ,  C08F6/003 ,  C08F10/00 ,  C08F110/02 ,  C08L23/00 ,  C08F2/14

Abstract: A manufacturing system for producing polyolefin includes a polymerization reactor, a flash chamber, and a purge column. In certain embodiments, the purge column may receive a solids stream directly from the flash chamber. Further, the purge column may function as a feed tank for an extruder within an extrusion/loadout system. According to certain embodiments, the manufacturing system may be configured to consume less than 445 kilowatt-hours of energy per metric ton of polyolefin produced based on consumption of electricity, steam, and fuel gas.

公开(公告)号：US08431032B2

公开(公告)日：2013-04-30

申请号：US12609330

申请日：2009-10-30

Applicant: Hee Young Kim ,  Kyung Koo Yoon ,  Yong Ki Park ,  Won Choon Choi

Inventor： Hee Young Kim ,  Kyung Koo Yoon ,  Yong Ki Park ,  Won Choon Choi

IPC: B44C1/22

CPC classification number: C30B29/06 ,  B01J8/1809 ,  B01J8/1827 ,  B01J8/1836 ,  B01J8/24 ,  B01J8/34 ,  B01J19/02 ,  B01J2208/00398 ,  B01J2208/00407 ,  B01J2208/00415 ,  B01J2208/00495 ,  B01J2208/00539 ,  B01J2208/0084 ,  B01J2208/00991 ,  B01J2219/0209 ,  B01J2219/0218 ,  B01J2219/0236 ,  B01J2219/0254 ,  B01J2219/0272 ,  B01J2219/029 ,  C01B33/027 ,  C30B28/14

Abstract: There is provided a method for continual preparation of granular polycrystalline silicon using a fluidized bed reactor, enabling a stable, long-term operation of the reactor by effective removal of silicon deposit accumulated on the inner wall of the reactor tube. The method comprises (i) a silicon particle preparation step, wherein silicon deposition occurs on the surface of the silicon particles, while silicon deposit is accumulated on the inner wall of the reactor tube encompassing the reaction zone; (ii) a silicon particle partial discharging step, wherein a part of the silicon particles remaining inside the reactor tube is discharged out of the fluidized bed reactor so that the height of the bed of the silicon particles does not exceed the height of the reaction gas outlet; and (iii) a silicon deposit removal step, wherein the silicon deposit is removed by supplying an etching gas into the reaction zone.

Abstract translation: 提供了一种使用流化床反应器连续制备颗粒状多晶硅的方法，通过有效去除积聚在反应器管内壁上的硅沉积物，能够稳定地长期运行反应器。 该方法包括：（i）硅颗粒制备步骤，其中在硅颗粒的表面上发生硅沉积，同时硅沉积物堆积在包围反应区的反应器管的内壁上; （ii）硅颗粒部分排出步骤，其中残留在反应器管内的硅颗粒的一部分从流化床反应器中排出，使得硅颗粒的床的高度不超过反应气体的高度 出口; 和（iii）硅沉积物去除步骤，其中通过向反应区域中提供蚀刻气体来除去硅沉积物。

公开(公告)号：US20120108876A1

公开(公告)日：2012-05-03

申请号：US13140933

申请日：2009-12-21

Applicant: Leslie Andrew Chewter ,  Jeroen Van Westrenen ,  Ferry Winter

Inventor： Leslie Andrew Chewter ,  Jeroen Van Westrenen ,  Ferry Winter

IPC: C07C1/20 ,  B01J19/00

CPC classification number: B01J8/1827 ,  B01J8/0055 ,  B01J8/26 ,  B01J19/02 ,  B01J2208/00176 ,  B01J2208/0084 ,  B01J2219/0004 ,  B01J2219/0218 ,  B01J2219/0236 ,  C07C1/20 ,  C10G2400/20 ,  C07C11/02

Abstract: A process and a reactor system for the preparation of an olefinic product by reacting an oxygenate feedstock in the presence of an oxygenate conversion catalyst within a reactor system under oxygenate-to-olefin conversion conditions, to obtain the olefinic product, wherein the reactor system has a contact surface coming in contact with oxygenates and wherein at least part of the contact surface is an material of the formula MX wherein: M is a metal and X is C, or M is a metal or Si and X is N.

Abstract translation: 一种用于制备烯烃产物的方法和反应器系统，其通过在含氧化合物 - 烯烃转化条件下的反应器系统内的含氧化合物转化催化剂存在下使含氧化合物原料反应得到烯烃产物，其中反应器体系具有 与氧化物接触的接触表面，并且其中至少部分接触表面是式MX的材料，其中：M是金属，X是C，或M是金属或Si，X是N.

公开(公告)号：US08128877B2

公开(公告)日：2012-03-06

申请号：US13207262

申请日：2011-08-10

Applicant: Robert R. McElvain ,  John D. Hottovy ,  Ralph W. Romig ,  Donald W. Verser ,  David H. Burns ,  John H. Tait ,  Richard Peacock ,  James E. Hein ,  Scott E. Kufeld ,  Carl W. Fenderson ,  Anurag Gupta ,  Dale A. Zellers ,  Penny A. Zellers, legal representative

Inventor： Robert R. McElvain ,  John D. Hottovy ,  Ralph W. Romig ,  Donald W. Verser ,  David H. Burns ,  John H. Tait ,  Richard Peacock ,  James E. Hein ,  Scott E. Kufeld ,  Carl W. Fenderson ,  Anurag Gupta ,  Dale A. Zellers

IPC: B01J10/00 ,  C08F2/00 ,  C08F210/00

CPC classification number: B01J19/0013 ,  B01J8/0015 ,  B01J19/1837 ,  B01J19/2455 ,  B01J2208/00212 ,  B01J2208/00752 ,  B01J2219/00006 ,  B01J2219/0236 ,  C08F2/01 ,  C08F6/003 ,  C08F10/00 ,  C08F110/02 ,  C08L23/00 ,  C08F2/14

Abstract: A manufacturing process for producing polyolefin, having a feed system, a reactor system including at least one polymerization reactor, a diluent/monomer recovery system, a fractionation system, and an extrusion/loadout system having an extruder. The manufacturing process is configured to consume less than 325 kilowatt-hours of electricity per metric ton of polyolefin produced.

Abstract translation: 具有进料系统的聚烯烃的制造方法，包括至少一个聚合反应器的反应器系统，稀释剂/单体回收系统，分馏系统和具有挤出机的挤出/压出系统。 制造过程被配置为每公吨生产的聚烯烃消耗少于325千瓦小时的电力。

公开(公告)号：US20110300025A1

公开(公告)日：2011-12-08

申请号：US13207262

申请日：2011-08-10

Applicant: Robert R. McElvain ,  John D. Hottovy ,  Ralph W. Romig ,  Donald W. Verser ,  David H. Burns ,  John H. Tait ,  Richard Peacock ,  James E. Hein ,  Scott E. Kufeld ,  Carl W. Fenderson ,  Anurag Gupta ,  Dale A. Zellers ,  Penny A. Zellers

Inventor： Robert R. McElvain ,  John D. Hottovy ,  Ralph W. Romig ,  Donald W. Verser ,  David H. Burns ,  John H. Tait ,  Richard Peacock ,  James E. Hein ,  Scott E. Kufeld ,  Carl W. Fenderson ,  Anurag Gupta ,  Dale A. Zellers ,  Penny A. Zellers

IPC: B01J19/00

CPC classification number: B01J19/0013 ,  B01J8/0015 ,  B01J19/1837 ,  B01J19/2455 ,  B01J2208/00212 ,  B01J2208/00752 ,  B01J2219/00006 ,  B01J2219/0236 ,  C08F2/01 ,  C08F6/003 ,  C08F10/00 ,  C08F110/02 ,  C08L23/00 ,  C08F2/14

Abstract: A manufacturing process for producing polyolefin, having a feed system, a reactor system including at least one polymerization reactor, a diluent/monomer recovery system, a fractionation system, and an extrusion/loadout system having an extruder. The manufacturing process is configured to consume less than 325 kilowatt-hours of electricity per metric ton of polyolefin produced.

Abstract translation: 具有进料系统的聚烯烃的制造方法，包括至少一个聚合反应器的反应器系统，稀释剂/单体回收系统，分馏系统和具有挤出机的挤出/压出系统。 制造过程被配置为每公吨生产的聚烯烃消耗少于325千瓦小时的电力。

公开(公告)号：US20110268645A1

公开(公告)日：2011-11-03

申请号：US13143094

申请日：2010-01-07

Applicant: Yutaka Mikawa ,  Makiko Kiyomi ,  Yuji Kagamitani ,  Toru Ishiguro

Inventor： Yutaka Mikawa ,  Makiko Kiyomi ,  Yuji Kagamitani ,  Toru Ishiguro

IPC: C30B7/10 ,  C01B21/06

CPC classification number: B01J19/02 ,  B01J2219/0236 ,  C30B7/105 ,  C30B29/403 ,  H01L21/02389 ,  H01L21/02425 ,  H01L21/02433 ,  H01L21/0254 ,  H01L21/0262 ,  Y10T117/1096

Abstract: To grow a highly pure nitride crystal having a low oxygen concentration efficiently by an ammonothermal method.A process for producing a nitride crystal, which comprises bringing a reactant gas reactive with ammonia to form a mineralizer, and ammonia into contact with each other to prepare a mineralizer in a reactor or in a closed circuit connected to a reactor; and growing a nitride crystal by an ammonothermal method in the presence of the ammonia and the mineralizer.

Abstract translation: 通过氨热法有效地生长具有低氧浓度的高纯度氮化物晶体。 一种制造氮化物晶体的方法，其包括使与氨反应形成矿化剂的反应物气体和氨彼此接触以在反应器或连接到反应器的闭路中制备矿化剂; 并在氨和矿化剂存在下通过氨热法生长氮化物晶体。

公开(公告)号：US07968048B2

公开(公告)日：2011-06-28

申请号：US11661910

申请日：2004-09-01

Applicant: Kevin S. Fraser ,  Murray Scott Pearson

Inventor： Kevin S. Fraser ,  Murray Scott Pearson

IPC: C21B7/16 ,  C21C5/48

CPC classification number: B01J19/02 ,  B01J4/001 ,  B01J2219/0236 ,  B01J2219/024

Abstract: A composite sparger for use in elevated temperature and corrosive environments. The composite sparger is formed from a thermally conductive non-combustible metal substrate. The surfaces of the conductive non-combustible metal exposed to the reactor environment are protected with a corrosion resistant layer. The corrosion resistant layer protects the substrate material from the corrosive environment of the reactor vessel and the substrate material conducts heat away from the corrosion resistant layer to prevent combustion of the corrosion resistant layer. The substrate material and corrosion resistant material may be selected so as to provide for sufficient thermal conduction to prevent combustion of the corrosion resistant material.

Abstract translation: 用于高温和腐蚀性环境的复合喷雾器。 复合喷雾器由导热不燃金属基底形成。 暴露于反应器环境的导电不可燃金属的表面用耐腐蚀层保护。 耐腐蚀层保护基板材料免受反应堆容器的腐蚀环境的影响，基板材料将热量从耐腐蚀层传导出去，以防止耐腐蚀层的燃烧。 可以选择衬底材料和耐腐蚀材料，以便提供足够的热传导以防止耐腐蚀材料的燃烧。

公开(公告)号：US20110027160A1

公开(公告)日：2011-02-03

申请号：US12903994

申请日：2010-10-13

Applicant: Javier San Segundo Sanchez ,  Jose Luis Montesinos Barona ,  Evaristo Ayuso Conejero ,  Manuel Vicente Vales Canle ,  Xavier Benevides Rel ,  Pedro-Tomas Lujan Garcia

Inventor： Javier San Segundo Sanchez ,  Jose Luis Montesinos Barona ,  Evaristo Ayuso Conejero ,  Manuel Vicente Vales Canle ,  Xavier Benevides Rel ,  Pedro-Tomas Lujan Garcia

IPC: C01B33/027

CPC classification number: C01B33/027 ,  B01J8/1827 ,  B01J8/24 ,  B01J19/02 ,  B01J2208/00407 ,  B01J2208/00415 ,  B01J2208/00433 ,  B01J2208/0046 ,  B01J2219/0236 ,  C01B33/029 ,  C01B33/03 ,  C01B33/035

Abstract: Methods and apparatus for the production of high purity silicon including a fluidized bed reactor with one or more protective layers deposited on an inside surface of the fluidized bed reactor. The protective layer may be resistant to corrosion by fluidizing gases and silicon-bearing gases.

Abstract translation: 包括生产高纯度硅的方法和装置，包括沉积在流化床反应器的内表面上的一个或多个保护层的流化床反应器。 保护层可以通过使气体和含硅气体流化而耐腐蚀。

公开(公告)号：US07875685B2

公开(公告)日：2011-01-25

申请号：US11936604

申请日：2007-11-07

Applicant: Kevin B. Stavens ,  Matthew W. Holtcamp ,  Gary D. Mohr ,  William A. Lamberti

Inventor： Kevin B. Stavens ,  Matthew W. Holtcamp ,  Gary D. Mohr ,  William A. Lamberti

IPC: C08F2/34 ,  B01J8/44 ,  C08F4/69

CPC classification number: B01J19/02 ,  B01J8/1818 ,  B01J8/44 ,  B01J2219/0236 ,  B01J2219/024 ,  B01J2219/0245 ,  C08F10/00 ,  Y10S526/901 ,  Y10T428/31692 ,  C08F2/004 ,  C08F2/01 ,  C08F2/34

Abstract: Apparatus and methods for gas phase polymerization are provided. The method can include polymerizing one or more olefins at gas phase conditions in a reactor comprising one or more process exposed surfaces in the presence of a catalyst system; and treating at least a portion of the one or more process exposed surfaces prior to injecting the catalyst system to reduce the number of surface hydroxyls or access of the catalyst system to the surface hydroxyls on the process exposed surfaces.

Abstract translation: 提供气相聚合的装置和方法。 该方法可以包括在气相条件下在催化剂体系存在下在包含一个或多个工艺暴露表面的反应器中聚合一种或多种烯烃; 以及在注入催化剂体系之前处理所述一个或多个工艺暴露表面的至少一部分以减少表面羟基的数量或催化剂体系进入工艺暴露表面上的表面羟基。