公开(公告)号：US20160374953A1

公开(公告)日：2016-12-29

申请号：US15261108

申请日：2016-09-09

Applicant: CRITITECH, INC.

Inventor： Michael BALTEZOR ,  Joseph FARTHING ,  Jake SITTENAUER ,  Jahna ESPINOSA ,  Samuel CAMPBELL ,  Matthew MCCLOREY ,  Julia K. FISCHER ,  Mark D. WILLIAMS

IPC: A61K9/51 ,  A61K31/337

CPC classification number: A61K31/337 ,  A61J3/02 ,  A61K9/0019 ,  A61K9/10 ,  A61K9/14 ,  A61K9/1605 ,  A61K9/1682 ,  A61K9/1688 ,  A61K9/5192 ,  B01D46/24 ,  B01D2271/02 ,  B01J2/04 ,  B01J3/008 ,  B01J3/02 ,  B01J4/002 ,  B01J19/10 ,  B01J19/26 ,  B05B1/3489 ,  B05B13/0278 ,  B05D2401/90

Abstract: Compositions are provided that include having at least 95% by weight of a taxane, or a pharmaceutically acceptable salt thereof, where the particles have a mean bulk density between about 0.050 g/cm3 and about 0.15 g/cm3, and/or a specific surface area (SSA) of at least 18 m2/g, 20 m2/g, 25 m2/g, 30 m2/g, 32 m2/g, 34 m2/g, or 35 m2/g. Methods for making and using such compositions are also provided.

Abstract translation: 提供的组合物包括具有至少95重量％的紫杉烷或其药学上可接受的盐，其中颗粒的平均堆积密度为约0.050g / cm 3至约0.15g / cm 3，和/或比表面积 面积（SSA）至少为18m2 / g，20m2 / g，25m2 / g，30m2 / g，32m2 / g，34m2 / g或35m2 / g。 还提供了制备和使用这些组合物的方法。

公开(公告)号：US09480933B2

公开(公告)日：2016-11-01

申请号：US14789665

申请日：2015-07-01

Applicant: LIST HOLDING AG

Inventor： Daniel Witte ,  Thomas Isenschmid ,  Manuel Steiner

IPC: C08F6/00 ,  B01D3/06 ,  C08F6/12 ,  B01J3/00 ,  B01J8/00 ,  C08J3/00

CPC classification number: B01D3/06 ,  B01J3/008 ,  B01J8/005 ,  C08F6/12

Abstract: A process for thermal separation of a solution comprised of a thermoplastic polymer and a solvent involves heating a solvent under pressure above a critical point of the solvent; decompressing the heated solvent in a first vessel, such that a polymer-rich and a low-polymer phase form; and supplying the polymer-rich phase to a second vessel. In embodiments, on entry into the second vessel, a pressure jump occurs, the pressure jump leading to a thermal flash in the second vessel such that a polymer part of the polymer-rich phase rises to at least 70%, and a resulting polymer-rich solution is provided.

Abstract translation: 用于热分解由热塑性聚合物和溶剂组成的溶液的方法包括在高于溶剂的临界点的压力下加热溶剂; 在第一容器中减压加热的溶剂，使得富聚合物和低聚合物相形式; 并将富聚合物相提供给第二容器。 在实施方案中，在进入第二容器时，发生压力跳跃，压力跳跃导致第二容器中的热闪光，使得富聚合物相的聚合物部分上升至至少70％，并且得到的聚合物 - 提供丰富的解决方案。

公开(公告)号：US20160229768A1

公开(公告)日：2016-08-11

申请号：US15067354

申请日：2016-03-11

Applicant: UOP LLC

Inventor： Robert L. Bedard ,  Christopher Naunheimer ,  Gavin P. Towler

IPC: C07C2/78

CPC classification number: C07C2/78 ,  B01F5/0475 ,  B01F15/063 ,  B01F2015/061 ,  B01J3/008 ,  B01J4/002 ,  B01J12/005 ,  B01J19/26 ,  B01J2219/00063 ,  B01J2219/00123 ,  C10G9/38 ,  C10G2400/20 ,  F23C3/00 ,  F23N5/022 ,  F23N5/102 ,  Y02P30/40 ,  C07C11/24

Abstract: Apparatus and methods are provided for converting methane in a feed stream to acetylene. A hydrocarbon stream is introduced into a supersonic reactor and pyrolyzed to convert at least a portion of the methane to acetylene. The reactor effluent stream may be treated to convert acetylene to another hydrocarbon process.

Abstract translation: 提供了将进料流中的甲烷转化为乙炔的装置和方法。 将烃流引入超音速反应器中并热解以将至少一部分甲烷转化为乙炔。 反应器流出物流可以被处理以将乙炔转化成另一个烃过程。

公开(公告)号：US20160228847A1

公开(公告)日：2016-08-11

申请号：US15131316

申请日：2016-04-18

Applicant: UOP LLC

Inventor： Carl J. Stevens ,  Antoine Negiz ,  Vinayender Kuchana

IPC: B01J19/26 ,  B01J19/24 ,  C07C2/78

CPC classification number: B01J19/26 ,  B01J3/008 ,  B01J4/002 ,  B01J6/008 ,  B01J19/02 ,  B01J19/2415 ,  B01J2219/0004 ,  B01J2219/00051 ,  B01J2219/00094 ,  B01J2219/00123 ,  B01J2219/00157 ,  B01J2219/0204 ,  B01J2219/0263 ,  B01J2219/0281 ,  B01J2219/0286 ,  B01J2219/029 ,  C07C2/78 ,  C07C11/24

Abstract: A pyrolytic reactor comprising a fuel injection zone, a combustion zone adjacent to the fuel injections zone, an expansion zone adjacent to the combustion zone, a feedstock injection zone comprising a plurality of injection nozzles and disposed adjacent to the expansion zone, a mixing zone configured to mix a carrier stream and feed material and disposed adjacent to the feedstock injection zone, and a reaction zone adjacent to the mixing zone. The plurality of injection nozzles are radially distributed in a first assembly defining a first plane transverse to the feedstock injection zone and in a second assembly transverse to the feedstock injection zone.

Abstract translation: 一种热解反应器，包括燃料喷射区域，与燃料喷射区域邻近的燃烧区域，与燃烧区域相邻的膨胀区域，包括多个喷嘴并且邻近膨胀区域设置的原料喷射区域，配置为 混合载体料流和进料，并与原料注入区相邻设置，以及与混合区相邻的反应区。 多个注射喷嘴径向分布在限定垂直于原料注射区的第一平面的第一组件中，并且横向于原料注入区的第二组件中。

公开(公告)号：US09382491B2

公开(公告)日：2016-07-05

申请号：US14146601

申请日：2014-01-02

Applicant: SarTec Corporation

Inventor： Clayton V. McNeff ,  Larry C. McNeff ,  Daniel Thomas Nowlan ,  Bingwen Yan ,  Peter G. Greuel

IPC: C10G3/00 ,  C10L3/08 ,  C10L1/02 ,  B01J8/08 ,  B01J8/10 ,  B01J19/20 ,  B01J3/00 ,  C11C3/00 ,  B01J38/02 ,  B01J21/06 ,  C10L3/10 ,  B01J21/20 ,  B01J35/00

CPC classification number: C10G3/44 ,  B01J3/008 ,  B01J8/087 ,  B01J8/10 ,  B01J19/20 ,  B01J21/06 ,  B01J21/066 ,  B01J21/20 ,  B01J35/0013 ,  B01J38/02 ,  B01J2208/00017 ,  B01J2208/00168 ,  B01J2208/00539 ,  B01J2208/00628 ,  B01J2208/00814 ,  B01J2219/00087 ,  B01J2219/00162 ,  B01J2219/00186 ,  C10G3/45 ,  C10G2300/805 ,  C10L1/02 ,  C10L1/023 ,  C10L1/04 ,  C10L3/08 ,  C10L3/106 ,  C10L2200/0469 ,  C10L2270/023 ,  C10L2290/06 ,  C10L2290/50 ,  C11C3/00 ,  Y02P20/544 ,  Y02P30/20

Abstract: Embodiments of the invention include apparatus and systems for hydrocarbon synthesis and methods regarding the same. In an embodiment, the invention includes a method for creating a hydrocarbon product stream comprising reacting a reaction mixture in the presence of a catalyst inside of a reaction vessel to form a product mixture, the reaction mixture comprising a carbon source and water. The temperature inside the reaction vessel can be between 450 degrees Celsius and 600 degrees Celsius and the pressure inside the reaction vessel can be above supercritical pressure for water. In an embodiment, the invention includes an extrusion reactor system for creating a hydrocarbon product stream. The temperature inside the extrusion reactor housing between 450 degrees Celsius and 600 degrees Celsius. Pressure inside the reaction vessel can be above supercritical pressure for water. Other embodiments are also included herein.

Abstract translation: 本发明的实施方案包括用于烃合成的装置和系统及其方法。 在一个实施方案中，本发明包括用于产生烃产物流的方法，包括在反应容器内的催化剂存在下使反应混合物反应以形成产物混合物，所述反应混合物包含碳源和水。 反应容器内的温度可以在450摄氏度至600摄氏度之间，反应容器内的压力可能超过水的超临界压力。 在一个实施方案中，本发明包括用于产生烃产物流的挤出反应器系统。 挤压反应器内部的温度在450摄氏度到600摄氏度之间。 反应容器内的压力可超过水的超临界压力。 本文还包括其它实施例。

公开(公告)号：US20160160137A1

公开(公告)日：2016-06-09

申请号：US14906530

申请日：2013-08-01

Applicant: EMPIRE TECHNOLOGY DEVELOPMENT LLC

Inventor： Aya SEIKE

IPC: C10J3/78 ,  C10J3/20 ,  C25D13/02 ,  C10J3/02

CPC classification number: C10J3/78 ,  B01J3/008 ,  B01J8/0005 ,  B01J19/02 ,  B01J2219/0218 ,  B01J2219/024 ,  C10J3/02 ,  C10J3/20 ,  C10J2300/093 ,  C10J2300/0979 ,  C10J2300/1853 ,  C25D13/02

Abstract: Provided herein are corrosion-resistant reactors that can be used for gasification, and methods of making and using the same. Some embodiments include a corrosion-resistant ceramic layer. According to some embodiments, the corrosion-resistant ceramic layer has a negative charge. At temperature above water's critical point (for example, 374CC and at 22.1 MPa I 218 atm), water can behave as an adjustable solvent and can have tunable properties depending on temperature and pressure.

Abstract translation: 本文提供了可用于气化的耐腐蚀反应器及其制造和使用方法。 一些实施例包括耐腐蚀陶瓷层。 根据一些实施例，耐腐蚀陶瓷层具有负电荷。 在高于水临界点的温度（例如374℃和22.1MPa I 218atm）下，水可以表现为可调溶剂，并且可以根据温度和压力具有可调谐的性质。

公开(公告)号：US09079984B2

公开(公告)日：2015-07-14

申请号：US13807400

申请日：2011-06-29

Applicant: Daniel Witte ,  Thomas Isenschmid ,  Manuel Steiner

Inventor： Daniel Witte ,  Thomas Isenschmid ,  Manuel Steiner

IPC: C08G63/00 ,  C08F6/12 ,  B01J3/00 ,  B01J8/00 ,  C08G63/02

CPC classification number: B01D3/06 ,  B01J3/008 ,  B01J8/005 ,  C08F6/12

Abstract: A process for thermal separation of a solution comprised of a thermoplastic polymer and a solvent involves heating a solvent under pressure above a critical point of the solvent; decompressing the heated solvent in a first vessel, such that a polymer-rich and a low-polymer phase form; and supplying the polymer-rich phase to a second vessel. In embodiments, on entry into the second vessel, a pressure jump occurs, the pressure jump leading to a thermal flash in the second vessel such that a polymer part of the polymer-rich phase rises to at least 70%, and a resulting polymer-rich solution is provided.

Abstract translation: 用于热分解由热塑性聚合物和溶剂组成的溶液的方法包括在高于溶剂的临界点的压力下加热溶剂; 在第一容器中减压加热的溶剂，使得富含聚合物和低聚合物相的形式; 并将富聚合物相提供给第二容器。 在实施方案中，在进入第二容器时，发生压力跳跃，压力跳跃导致第二容器中的热闪光，使得富聚合物相的聚合物部分上升至至少70％，并且得到的聚合物 - 提供丰富的解决方案。

公开(公告)号：US20150105586A1

公开(公告)日：2015-04-16

申请号：US14576084

申请日：2014-12-18

Applicant: UOP LLC

Inventor： Jeffery C. Bricker ,  John Q. Chen ,  Peter K. Coughlin

IPC: C07C51/00 ,  B01J19/10 ,  C07C51/10

CPC classification number: C07C51/00 ,  B01F5/0475 ,  B01F15/063 ,  B01F2015/061 ,  B01J3/008 ,  B01J4/002 ,  B01J12/005 ,  B01J12/007 ,  B01J19/10 ,  B01J19/26 ,  B01J2204/002 ,  B01J2219/00006 ,  B01J2219/0875 ,  C07C2/06 ,  C07C2/82 ,  C07C5/09 ,  C07C6/04 ,  C07C45/35 ,  C07C51/10 ,  C07C51/252 ,  C07C47/22 ,  C07C57/04 ,  C07C11/24 ,  C07C11/04 ,  C07C11/08 ,  C07C11/06

Abstract: Methods and systems are provided for converting methane in a feed stream to acetylene. The method includes processing the acetylene to form a stream having acrylic acid. The hydrocarbon stream is introduced into a supersonic reactor and pyrolyzed to convert at least a portion of the methane to acetylene. The reactor effluent stream is be treated to convert acetylene to acrylic acid. The method according to certain aspects includes controlling the level of carbon monoxide to prevent undesired reactions in downstream processing units.

Abstract translation: 提供了将进料流中的甲烷转化为乙炔的方法和系统。 该方法包括加工乙炔以形成具有丙烯酸的料流。 将烃流引入超音速反应器中并热解以将至少一部分甲烷转化为乙炔。 处理反应器流出物流将乙炔转化为丙烯酸。 根据某些方面的方法包括控制一氧化碳的水平以防止下游处理单元中的不期望的反应。

公开(公告)号：US08961780B1

公开(公告)日：2015-02-24

申请号：US14107471

申请日：2013-12-16

Applicant: Saudi Arabian Oil Company

Inventor： Zaki Yusuf ,  Ahmad D. Hammad ,  Stamatios Souentie ,  Bandar Fadhel ,  Nayif Rasheedi

IPC: C10G21/12 ,  C07C7/10

CPC classification number: C10G21/28 ,  B01D11/0403 ,  B01J3/008 ,  C07C7/10 ,  C07D207/00 ,  C10G21/08 ,  C10G2300/202 ,  C10G2300/205 ,  C10G2300/44

Abstract: Methods for recovering organic heteroatom compounds from a hydrocarbon feedstock include feeding into a contactor a hydrocarbon feedstock and an aqueous solvent to form an extraction mixture of the aqueous solvent with the hydrocarbon feedstock. The hydrocarbon feedstock includes a hydrocarbon and an organic heteroatom compound. The aqueous solvent includes an ionic liquid formed from pressurized carbon dioxide and water. A pressure and temperature of the extraction mixture may be established that together tune the aqueous solvent to selectively form a solvent complex with the at least one organic heteroatom compound. Then, the solvent complex is extracted to a recovery vessel from the extraction mixture in the contactor. By adjustment of a recovery temperature of the recovery vessel, a recovery pressure of the recovery vessel, or both, the solvent complex decomposes into carbon dioxide and the organic heteroatom compound. The organic heteroatom compound is then recovered from the recovery vessel.

Abstract translation: 从烃原料中回收有机杂原子化合物的方法包括将烃原料和含水溶剂进料到接触器中以形成含水溶剂与烃原料的萃取混合物。 烃原料包括烃和有机杂原子化合物。 含水溶剂包括由加压二氧化碳和水形成的离子液体。 可以建立萃取混合物的压力和温度，其一起调节水性溶剂以选择性地与至少一种有机杂原子化合物形成溶剂配合物。 然后，将溶剂配合物从接触器中的萃取混合物中提取回收容器。 通过调节回收容器的回收温度，回收容器的回收压力或二者，溶剂配合物分解成二氧化碳和有机杂原子化合物。 然后从回收容器中回收有机杂原子化合物。

公开(公告)号：US20140334985A1

公开(公告)日：2014-11-13

申请号：US14338749

申请日：2014-07-23

Applicant: Saudi Arabian Oil Company

Inventor： Ki-Hyouk Choi

IPC: B01J3/00

CPC classification number: B01J3/008 ,  C10G9/00 ,  C10G31/08 ,  C10G45/26 ,  C10G47/32 ,  C10G75/00 ,  C10G2300/1033 ,  C10G2300/202 ,  C10G2300/205 ,  C10G2300/206 ,  C10G2300/4081 ,  C10G2300/805 ,  E21B43/16

Abstract: A continuous process to upgrade heavy crude oil for producing more valuable crude feedstock having high API gravity, low asphaltene content, and high middle distillate yield, low sulfur content, low nitrogen content, and low metal content without external supply of hydrogen and/or catalyst. Heavy crude oil having substantial amount of asphaltene and heavy components is mixed with highly waxy crude oil having large amount of paraffinic components and water to decompose asphaltene compounds and remove sulfur, nitrogen, and metal containing substances under supercritical conditions. Product has higher API gravity, lower asphaltene content, high middle distillate yield, lower sulfur content, lower nitrogen content, and lower metal content to be suitable for conventional petroleum refining process.

Abstract translation: 连续加工重质原油，用于生产更有价值的原油原料，具有高API重力，低沥青质含量和高中间馏分产率，低硫含量，低氮含量和低金属含量，无需外部供应氢气和/或催化剂 。 将具有大量沥青质和重质成分的重质原油与具有大量链烷烃成分和水的高度蜡质原油混合，以分解沥青质化合物并在超临界条件下除去含硫，氮和金属的物质。 产品具有较高的API重力，较低的沥青质含量，较高的中间馏分产率，较低的硫含量，较低的氮含量和较低的金属含量适用于常规的石油炼制过程。