公开(公告)号：EP3478798B1

公开(公告)日：2020-09-16

申请号：EP17729307.3

申请日：2017-05-30

Applicant: ExxonMobil Research and Engineering Company

Inventor： SHIH, Stuart, S. ,  HILBERT, Timothy, L. ,  SKOULIDAS, Anastasios, l. ,  PATEL, Bryan, A. ,  CHUBA, Michael, R. ,  SMYTH, Sean, C. ,  KALYANARAMAN, Mohan

IPC: C10G45/62 ,  C10G45/64 ,  C10G45/02 ,  C10G65/04 ,  B01J29/70

公开(公告)号：EP1853369A1

公开(公告)日：2007-11-14

申请号：EP06719236.9

申请日：2006-01-23

Applicant: EXXONMOBIL RESEARCH AND ENGINEERING COMPANY

Inventor： SCHORFHEIDE, James, J. ,  SMYTH, Sean, C. ,  KAUL, Bal, K. ,  STERN, David, L.

IPC: B01D53/047 ,  C10G45/02 ,  C10G45/04

CPC classification number: C10G45/04

Abstract: This invention relates to an improved hydrotreating process for removing sulfur from naphtha and distillate feedstreams. This improved process utilizes a hydrotreating zone, an acid gas removal zone, and a pressure swing adsorption zone having a total cycle time of less than about 30 seconds for increasing the concentration of hydrogen utilized in the process.

公开(公告)号：EP1853368A1

公开(公告)日：2007-11-14

申请号：EP06719235.1

申请日：2006-01-23

Applicant: EXXONMOBIL RESEARCH AND ENGINEERING COMPANY

Inventor： SABOTTKE, Craig, Y. ,  CORCORAN, Edward, W. ,  ECKES, Richard, L. ,  KAUL, Bal, K. ,  SUNDARAM, Narasimhan ,  SCHORFHEIDE, James, J. ,  SMYTH, Sean, C. ,  STERN, David, L.

IPC: B01D53/047 ,  C10G45/02 ,  C10G45/58 ,  C10G47/00 ,  C10G45/32 ,  C10G45/44

CPC classification number: C10G47/00 ,  B01D53/0462 ,  B01D53/047 ,  B01D53/261 ,  B01D2253/102 ,  B01D2253/106 ,  B01D2253/108 ,  B01D2253/116 ,  B01D2256/16 ,  B01D2257/102 ,  B01D2257/502 ,  B01D2257/504 ,  B01D2257/702 ,  B01D2257/7025 ,  B01D2257/80 ,  B01D2259/40007 ,  B01D2259/4003 ,  B01D2259/40041 ,  B01D2259/40052 ,  B01D2259/40067 ,  B01D2259/40073 ,  B01D2259/40081 ,  B01D2259/402 ,  B01D2259/406 ,  B01D2259/4062 ,  B01D2259/414 ,  C10G45/02 ,  C10G45/32 ,  C10G45/44 ,  C10G45/58 ,  C10G2300/1022 ,  C10G2300/1044 ,  C10G2300/1051 ,  C10G2300/1055 ,  C10G2300/107 ,  C10G2300/1074 ,  C10G2300/1077 ,  C10G2300/202 ,  C10G2300/207 ,  C10G2300/4081 ,  C10G2300/42 ,  Y02C10/08 ,  Y02C20/20

Abstract: Improved hydroprocessing processes for upgrading refinery streams via the use of rapid cycle pressure swing absorption having a cycle time of less than 30 s for increasing the concentration of hydrogen in the vapor phase product recycled to the hydroprocessing zone.

公开(公告)号：EP3478798A1

公开(公告)日：2019-05-08

申请号：EP17729307.3

申请日：2017-05-30

Applicant: ExxonMobil Research and Engineering Company

Inventor： SHIH, Stuart, S. ,  HILBERT, Timothy, L. ,  SKOULIDAS, Anastasios, l. ,  PATEL, Bryan, A. ,  CHUBA, Michael, R. ,  SMYTH, Sean, C. ,  KALYANARAMAN, Mohan

IPC: C10G45/62 ,  C10G45/64 ,  C10G45/02 ,  C10G65/04 ,  B01J29/70

Abstract: Systems and methods are provided for catalytically dewaxing a diesel boiling range feed. In some aspects, catalytic dewaxing can be performed at low hydrogen treat gas rates and/or low hydrogen purity conditions. In other aspects, the systems and methods can allow for distillate dewaxing while reducing or minimizing the amount of equipment required.

公开(公告)号：EP1858829A2

公开(公告)日：2007-11-28

申请号：EP06736480.2

申请日：2006-02-28

Applicant: EXXONMOBIL RESEARCH AND ENGINEERING COMPANY

Inventor： UMANSKY, Benjamin, Santiago ,  CLARK, Michael, christopher ,  LOPEZ, Carlos, N. ,  VIETS, John, Werner ,  SMITH, C., Morris ,  THURTELL, John, Harland ,  MELLI, Tomas, R. ,  SMYTH, Sean, C.

IPC: C07C2/68

CPC classification number: C07C2/66 ,  C10G11/18 ,  C10G29/205 ,  C10G50/00 ,  C10G57/005 ,  C10G2300/1092 ,  C10G2300/1096 ,  C10G2300/202 ,  C10G2300/301 ,  C10G2300/305 ,  C10G2300/4018 ,  C10G2400/02 ,  C10L1/06 ,  C10L2200/0415 ,  C10L2200/0423

Abstract: Solid phosphoric acid (SPA) olefin oligomerization process units may be converted to operation with a more environmentally favorable solid catalyst. The SPA units in which a light olefin feed is oligomerized to form gasoline boiling range hydrocarbon product, is converted unit to operation with a molecular sieve based olefin oligomerization catalyst comprising an MWW zeolite material. Besides being more environmentally favorable in use, the MWW based zeolites offer advantages in catalyst cycle life, selectivity. After loading of the catalyst, the converted unit is operated as a fixed-bed unit by passing a C 2 - C 4 olefinic feed and a light aromatic co-feed containing benzene to a fixed bed of the MWW zeolite catalyst to effect alkylation of the benzene with the aromatic co-feed, typically at a temperature from 150 to 350° C., a pressure not greater than 7000 kpa, usually less than 4000 kPa and an olefin space velocity up to 10 WHSV.