公开(公告)号：US20190338193A1

公开(公告)日：2019-11-07

申请号：US15972657

申请日：2018-05-07

Applicant: David J. McCutchen

Inventor： David J. McCutchen

IPC: C10B1/10 ,  B01J8/08 ,  B01J8/00 ,  C10B27/00 ,  B01D45/16 ,  B03C3/00

Abstract: A shear retort mill for slow ablative pyrolysis features friction heating between shearing surfaces on a rotating disk and a static or rotating cylindrical drum enclosing the disk. A feed enters the workspace between the rotating disk and the bottom of the drum through a hollow feed shaft coupled to the rotating disk. Preferably, an auger compacts and moves the feed downward, and a shredder reduces the feed's particle size. The feed is increasingly ground and pyrolyzed as it is forced between the drum and disk shearing surface. As the dense processed material extrudes at the edge of the workspace, the gases and liquid products are forced inward by the barrier of dense solids. A static exhaust pipe at the center of the rotating feed shaft allows for the exit of these gases, which preferably go to a heat exchanger to recover any condensable fractions.

公开(公告)号：US10363535B1

公开(公告)日：2019-07-30

申请号：US15956030

申请日：2018-04-18

Applicant: SHANGHAI YANKUANG ENERGY R&D CO., LTD.

Inventor： Qiwen Sun ,  Jianmin Wu ,  Liang Dong ,  Zongsen Zhang ,  Jisen Liu ,  Jianping Yue ,  Fang Yan

IPC: B01J8/08 ,  C10G2/00 ,  B01J8/22 ,  B01J8/00

Abstract: A gas-liquid-solid three-phase slurry bed industrial reactor capable of achieving continuous operation comprises an inlet gas distribution component composed of a false bottom and inlet gas distribution tubes, one or more layers of heat exchange tube components used for heating/cooling the bed, one or more layers of liquid-solid separator components capable of being cleaned automatically, an outlet gas-liquid-solid entrainment separation component located in the upper portion of the interior of the reactor and used for removing liquid foam and solid entrainments, a plurality of layers of solid concentration uniform distribution devices used for reducing the catalyst concentration gradient and the inlet-outlet temperature difference of the reactor, a flow guiding device located on a component support beam and used for preventing catalyst accumulation, and auxiliary systems including a filter-backflush system and a washing system. Compared with the prior art, the reactor is low in energy consumption and solves the problems of blockage, backflow and dead zones, the temperature and liquid level are well controlled, catalysts can be easily added and discharged online, and stable and continuous operation of the reactor is achieved. The reactor is suitable for being applied to the Fischer-Tropsch synthesis process on an industrial scale.

公开(公告)号：US20190225563A1

公开(公告)日：2019-07-25

申请号：US16255364

申请日：2019-01-23

Applicant: Dow Global Technologies LLC

Inventor： Matthew T. Pretz

IPC: C07C5/333 ,  B01J23/26 ,  B01J38/02 ,  B01J38/12 ,  B01J38/14 ,  B01J23/62 ,  B01J23/94 ,  B01J35/00 ,  B01J21/04 ,  B01J21/12 ,  B01J23/887 ,  B01J23/92 ,  B01J23/96 ,  B01J35/10 ,  B01J8/00 ,  B01J8/26 ,  B01J8/18 ,  B01J8/12 ,  B01J8/08

CPC classification number: C07C5/3332 ,  B01J8/0025 ,  B01J8/0055 ,  B01J8/087 ,  B01J8/12 ,  B01J8/1836 ,  B01J8/1863 ,  B01J8/26 ,  B01J21/04 ,  B01J21/12 ,  B01J23/26 ,  B01J23/62 ,  B01J23/8871 ,  B01J23/92 ,  B01J23/94 ,  B01J23/96 ,  B01J35/0006 ,  B01J35/1009 ,  B01J35/1014 ,  B01J38/02 ,  B01J38/12 ,  B01J38/14 ,  B01J2208/00176 ,  B01J2208/00362 ,  B01J2208/00769 ,  B01J2219/00024 ,  C07C2521/04 ,  C07C2521/08 ,  C07C2521/12 ,  C07C2523/08 ,  C07C2523/42 ,  C07C2523/62 ,  Y02P20/125 ,  Y02P20/52 ,  Y02P20/584 ,  C07C11/06 ,  C07C11/08

Abstract: An integrated process for producing C3-C4 olefins or di-olefins including: contacting a hydrocarbon feed and a catalyst feed in a fluidized dehydrogenation reactor under conditions such that a product mixture is formed and the catalyst is at least partially deactivated; transferring the product mixture and the catalyst from the reactor to a cyclonic separation system under conditions such that the product mixture is converted to form a new product mixture and is separated from the catalyst; transferring at least a portion of the catalyst to a regenerator vessel and heating it in order to combust the coke deposited thereon; subjecting the catalyst to a conditioning step to form an oxygen-containing, at least partially reactivated catalyst; and transferring the partially reactivated catalyst back to the fluidized dehydrogenation reactor.

公开(公告)号：US20190210888A1

公开(公告)日：2019-07-11

申请号：US16352466

申请日：2019-03-13

Applicant: Tronox LLC

Inventor： Harry E. Flynn

IPC: C01G23/07 ,  C01G23/02 ,  B01J8/08

CPC classification number: C01G23/07 ,  B01J8/08 ,  B01J8/14 ,  B01J2208/00495 ,  B01J2208/00752 ,  B01J2208/00761 ,  B01J2208/00769 ,  B01J2219/0218 ,  B01J2219/024 ,  C01G23/022

Abstract: A metal chloride generator is provided. The metal chloride generator is a metal chloride centrifugal reactor that can be operated under conditions sufficient to cause metal particles and chlorine in the generator to be brought into contact with one another and react using centrifugal force to form metal chloride. A process for manufacturing titanium dioxide that utilizes the metal chloride generator is also provided.

公开(公告)号：US10308516B2

公开(公告)日：2019-06-04

申请号：US14990431

申请日：2016-01-07

Applicant: MITSUBISHI CHEMICAL CORPORATION ,  THE UNIVERSITY OF TOKYO

Inventor： Tatsuya Okubo ,  Toru Wakihara ,  Zhendong Liu ,  Takahiko Takewaki ,  Kazunori Oshima ,  Daisuke Nishioka

IPC: C01B39/54 ,  C01B39/48 ,  B01J29/70 ,  B01J29/83 ,  C01B39/10 ,  B01J29/06 ,  C01B39/02 ,  B01J29/85 ,  B01J8/08 ,  B01J29/76 ,  C01B39/04 ,  C01B39/46 ,  B01J19/24

Abstract: Provided is a method for continuous production of zeolite in which a starting material is continuously supplied to a tubular reactor to produce an aluminophosphate zeolite that contains, in the framework structure, at least aluminum atoms and phosphorus atoms or an aluminosilicate zeolite having 5≤SiO2/Al2O3≤2000. The tubular reactor is heated using a heat medium; a ratio (volume)/(lateral surface area) of the volume (inner capacity) to the lateral surface area of the tubular reactor is 0.75 cm or smaller; and seed crystals are added to the starting material. Through using a small-diameter tubular reactor and heating with a heat medium, it becomes possible to heat sufficiently the entirety of a starting material (zeolite precursor gel) in a short time, and to allow reaction to proceed at a high rate. The occurrence of irregular pressure fluctuations during continuous production of the zeolite can be prevented by adding seed crystals.

公开(公告)号：US20190128612A1

公开(公告)日：2019-05-02

申请号：US16234170

申请日：2018-12-27

Applicant: Thar Energy LLC

Inventor： Lalit Chordia ,  John C. Davis

IPC: F28D7/16 ,  B01J19/00 ,  B01J19/24 ,  F28F9/02 ,  B01J8/08

Abstract: Counter-flow heat exchanged is constructed with plenums at either end that separate the opposing fluids, the channels of which are arrayed in a checkerboard patterns, such that any given channel is surrounded by channels of opposing streams on four sides—laterally on both sides and vertically above and below.

公开(公告)号：US20190122779A1

公开(公告)日：2019-04-25

申请号：US16227848

申请日：2018-12-20

Applicant: Studsvik, Inc.

Inventor： J. Bradley Mason ,  Walter Scott Roesener

IPC: G21F9/00 ,  G21F9/32 ,  G21F9/02 ,  B01D53/04 ,  B01D39/20 ,  G21F9/12 ,  G21F9/30 ,  F23G7/06 ,  B01J8/24 ,  B01J8/08 ,  B01J8/18

CPC classification number: G21F9/00 ,  B01D39/2034 ,  B01D39/2075 ,  B01D53/04 ,  B01D2257/20 ,  B01D2257/30 ,  B01D2258/02 ,  B01D2259/40001 ,  B01J8/087 ,  B01J8/1836 ,  B01J8/24 ,  B01J2208/00017 ,  B01J2208/00823 ,  F23G7/061 ,  G21F9/02 ,  G21F9/12 ,  G21F9/30 ,  G21F9/32

Abstract: Treatment of radioactive waste comprising organic compounds, and sulfur-containing compounds and/or halogen-containing compounds. An apparatus comprises a reaction vessel comprising a filter for carrying out thermal treatment of the waste and a thermal oxidizer. Utilizing co-reactants to reduce gas phase sulfur and halogen from treatment of wastes.

公开(公告)号：US20190077912A1

公开(公告)日：2019-03-14

申请号：US15798401

申请日：2017-10-31

Applicant: National Tsing Hua University ,  Chang Chun Plastics Co., Ltd. ,  Chang Chun Petrochemical Co., Ltd.

Inventor： David S. H. Wong ,  Kan-Nan Chan ,  Ping-Lin Yang ,  An-Pang Tu ,  En-Ko Lee

IPC: C08G71/04 ,  B01J8/08

Abstract: A preparation method of a polyurethane resin including the following steps is provided. A liquid polyamine compound is placed in a continuous reaction system, and the liquid polyamine compound is circulated in the continuous reaction system. A solid bis(cyclic carbonate) and a solid catalyst are placed in the continuous reaction system to mix the solid bis(cyclic carbonate), solid catalyst, and liquid polyamine compound to form a heterogeneous mixture. The heterogeneous mixture is heated in the continuous reaction system in a microwave manner, such that the heterogeneous mixture reacts to form a polyurethane resin.

公开(公告)号：US10150054B1

公开(公告)日：2018-12-11

申请号：US15827410

申请日：2017-11-30

Applicant: Technip Process Technology, Inc.

Inventor： Paul Marchant ,  Raj Kanwar Singh

IPC: B01J8/00 ,  B01J8/08 ,  B01J8/18 ,  B01J8/24 ,  B01J8/34 ,  B01J8/38 ,  B01J19/32 ,  B01D15/18 ,  B01D53/12

Abstract: A packing system is disclosed that has a series of flat blades arranged to promote mixing in a fluidized bed such as one in a FCC stripper, with an upward flowing gas stream and a downward flowing solid particle stream. The blade arrangement provides for different gas solids flow directions within a single layer of packing system to enhance cross mixing of gas and catalyst in all directions and reduces the potential for gas and catalyst bypassing. The blade arrangement has splits which minimizes the tendency for phase separation around the blade. The arrangement and sizing of the blades is intended to promote intimate contact between the two phases to ensure efficient mass transfer of material trapped inside the particles to the gas phase. The arrangement of the blades prevents excessive bubble growth and channeling, both of which reduce surface area for mass transfer.

公开(公告)号：US10144879B2

公开(公告)日：2018-12-04

申请号：US15189428

申请日：2016-06-22

Applicant: SarTec Corporation

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

IPC: C10G3/00 ,  C10L1/02 ,  C10L3/08 ,  B01J8/08 ,  B01J8/10 ,  B01J19/20 ,  B01J3/00 ,  C11C3/00 ,  B01J38/02 ,  B01J21/06 ,  B01J35/00 ,  C10L1/04 ,  C10L3/10 ,  B01J21/20

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.