公开(公告)号：US20250019604A1

公开(公告)日：2025-01-16

申请号：US18898849

申请日：2024-09-27

Applicant: Chevron U.S.A. Inc.

Inventor： Ling JIAO ,  Bi-Zeng ZHAN ,  Don BUSHEE ,  Theodorus Ludovicus Michael MAESEN ,  Hye-Kyung TIMKEN ,  Richard DUTTA ,  Jay PAREKH

IPC: C10G65/12 ,  C10G7/00 ,  C10G47/14

Abstract: Provided is a hydrocracking process with a recycle loop for converting a petroleum feed to lower boiling products, which process comprises reacting a stream over a non-zeolite noble metal catalyst at a temperature of about 650° F. (343° C.) or less in a reactor positioned in the recycle loop of the hydrocracking reactor.

公开(公告)号：US20240101913A1

公开(公告)日：2024-03-28

申请号：US18270202

申请日：2021-12-29

Applicant: CHEVRON U.S.A. INC.

Inventor： Ling JIAO ,  Bi-Zheng ZHAN ,  Don BUSHEE ,  Theodorus Ludovicus Michael MAESEN ,  Hye-Kyung TIMKEN ,  Richard DUTTA ,  Jay PAREKH

IPC: C10G65/12 ,  C10G7/00 ,  C10G47/14

CPC classification number: C10G65/12 ,  C10G7/00 ,  C10G47/14 ,  C10G2300/107 ,  C10G2300/1074 ,  C10G2300/4006 ,  C10G2300/4081

Abstract: Provided is a hydrocracking process with a recycle loop for converting a petroleum feed to lower boiling products, which process comprises reacting a stream over a non-zeolite noble metal catalyst at a temperature of about 650° F. (343° C.) or less in a reactor positioned in the recycle loop of the hydrocracking reactor.

公开(公告)号：US20170051087A1

公开(公告)日：2017-02-23

申请号：US14829987

申请日：2015-08-19

Applicant: Chevron Phillips Chemical Company LP ,  Chevron U.S.A. Inc.

Inventor： Steven M. BISCHOF ,  Robert C. COFFIN ,  Kenneth D. HOPE ,  Michael S. DRIVER ,  Hye-Kyung TIMKEN

IPC: C08F110/14 ,  C07C5/03 ,  B01J31/02 ,  C07C2/26

CPC classification number: C08F110/14 ,  B01J31/0231 ,  B01J31/0279 ,  B01J31/0284 ,  B01J2231/20 ,  C07C2/22 ,  C07C2/26 ,  C07C5/03 ,  C07C2527/08 ,  C07C2527/11 ,  C07C2527/125 ,  C07C2531/02 ,  C10G50/00 ,  C10G50/02 ,  C07C11/02 ,  C07C9/22

Abstract: Disclosed herein are embodiments of a process which generally includes contacting i) a monomer or mixture of monomers, ii) a haloaluminate ionic liquid, and iii) one or more halide components in a reaction zone, and oligomerizing the monomer or mixture of monomers in the reaction zone to form an oligomer product. The combination of the haloaluminate ionic liquid and halide component can constitute a catalyst system which is used in embodiments of the process to produce the oligomer product.

Abstract translation: 本文公开了一种方法的实施方案，其通常包括使i）单体或单体混合物，ii）卤化铝离子液体，和iii）反应区域中的一种或多种卤化物组分，并使单体或单体混合物在 反应区形成低聚物产物。 卤代铝离子液体和卤化物组分的组合可以构成催化剂体系，其用于生产低聚物产物的方法的实施方案中。

公开(公告)号：US20230348289A1

公开(公告)日：2023-11-02

申请号：US18344530

申请日：2023-06-29

Applicant: Chevron U.S.A. Inc.

Inventor： Kandaswamy JOTHIMURUGESAN ,  Hye-Kyung TIMKEN

IPC: C01F7/34 ,  B01J21/12 ,  B01J35/10 ,  B01J37/03 ,  B01J37/04

CPC classification number: C01F7/34 ,  B01J21/12 ,  B01J35/1019 ,  B01J35/1047 ,  B01J35/1061 ,  B01J37/031 ,  B01J37/04 ,  C01P2002/72 ,  C01P2006/12 ,  C01P2006/14 ,  C01P2006/16

Abstract: A process of making a silica-alumina composition having improved properties is provided. The process includes (a) mixing an aqueous solution of a silicon compound and an aqueous solution of an aluminum compound and an acid, while maintaining a pH of the mixed solution in a range of 1 to 3, and obtaining an acidified silica-alumina sol; (b) adding an aqueous solution of a base precipitating agent to the acidified silica-alumina sol to a final pH in a range of 5 to 8, and co-precipitating a silica-alumina slurry, wherein the base precipitating agent is selected from ammonium carbonate, ammonium bicarbonate, and any combination thereof; (c) optionally, hydrothermally aging the silica-alumina slurry to form a hydrothermally aged silica-alumina slurry; and (d) recovering a precipitate solid from the silica-alumina slurry or the hydrothermally aged silica-alumina slurry, wherein the precipitate solid comprises the silica-alumina composition.

公开(公告)号：US20220153603A1

公开(公告)日：2022-05-19

申请号：US17382441

申请日：2021-07-22

Applicant: CHEVRON U.S.A. INC.

Inventor： Kandaswamy JOTHIMURUGESAN ,  Hye-Kyung TIMKEN

IPC: C01F7/34 ,  B01J21/12 ,  B01J37/04 ,  B01J37/03 ,  B01J35/10

Abstract: A process of making a silica-alumina composition having improved properties is provided. The process includes (a) mixing an aqueous solution of a silicon compound and an aqueous solution of an aluminum compound and an acid, while maintaining a pH of the mixed solution in a range of 1 to 3, and obtaining an acidified silica-alumina sol; (b) adding an aqueous solution of a base precipitating agent to the acidified silica-alumina sol to a final pH in a range of 5 to 8, and co-precipitating a silica-alumina slurry, wherein the base precipitating agent is selected from ammonium carbonate, ammonium bicarbonate, and any combination thereof; (c) optionally, hydrothermally aging the silica-alumina slurry to form a hydrothermally aged silica-alumina slurry; and (d) recovering a precipitate solid from the silica-alumina slurry or the hydrothermally aged silica-alumina slurry, wherein the precipitate solid comprises the silica-alumina composition.

公开(公告)号：US20160096784A1

公开(公告)日：2016-04-07

申请号：US14966208

申请日：2015-12-11

Applicant: Chevron U.S.A. Inc. ,  Chevron Phillips Chemical Company LP

Inventor： Lei JI ,  Ai-Fu CHANG ,  Michael S. DRIVER ,  Hye-Kyung TIMKEN

IPC: C07C7/11 ,  C07C7/144 ,  C07C7/00 ,  B01D53/14 ,  B01D53/22

CPC classification number: C07C7/11 ,  B01D53/14 ,  B01D53/1462 ,  B01D53/1468 ,  B01D53/1475 ,  B01D53/1487 ,  B01D53/1493 ,  B01D53/229 ,  B01D53/52 ,  B01D53/526 ,  B01D53/62 ,  B01D53/72 ,  B01D53/78 ,  B01D2252/20426 ,  B01D2252/20473 ,  B01D2252/30 ,  B01D2256/22 ,  B01D2256/24 ,  B01D2257/304 ,  B01D2257/504 ,  B01D2257/7022 ,  C01B17/167 ,  C01B31/20 ,  C01B32/50 ,  C07C7/005 ,  C07C7/144 ,  C07C7/152 ,  C07C7/156 ,  Y02P20/152 ,  Y02P20/542 ,  C07C9/12 ,  C07C11/04

Abstract: Disclosed are systems and methods which provide a process stream comprising a gaseous component, capture the gaseous component from the process stream by an ionic liquid solvent of a separator, and recover a captured gaseous component from the ionic liquid solvent in a regenerator. A second gaseous component from the process stream may be captured by the ionic liquid solvent of the separator, and the second gaseous component may be recovered from the ionic liquid solvent in the regenerator. Alternatively, the second gaseous component from the process stream may be uncaptured by the ionic liquid solvent, and the uncaptured second gaseous component may be recovered from a membrane unit.