公开(公告)号：WO2014078226A1

公开(公告)日：2014-05-22

申请号：PCT/US2013/069398

申请日：2013-11-11

Applicant: PHILLIPS 66 COMPANY ,  PAUL, Uchenna P. ,  RANDOLPH, Bruce B. ,  NELSON, Jon M. ,  FJARE, Kristi A. ,  SMITH, Danielle K. ,  CRAGUN, Mark Rumel ,  SADOK, Richard D.

Inventor： RANDOLPH, Bruce B. ,  FJARE, Kristi A. ,  SMITH, Danielle K. ,  CRAGUN, Mark Rumel ,  SADOK, Richard D.

IPC: C01B3/16

CPC classification number: C01B3/323 ,  C01B2203/0233 ,  C01B2203/0405 ,  C01B2203/0415 ,  C01B2203/043 ,  C01B2203/1041 ,  C01B2203/1058 ,  C01B2203/1076 ,  C01B2203/1082 ,  C01B2203/1094 ,  C01B2203/1211 ,  C01B2203/1217 ,  C01B2203/1223 ,  C01B2203/1229

Abstract: A process is described for flowing an oxygenate feed over a catalyst in an adiabatic fixed bed reactor to product a reactor effluent and heat. The reaction inside the adiabatic fixed bed reactor occurs at a reaction temperature from about 200 ∘ C to about 375 ∘ C. The reactor effluent is then condensed to separate the liquid products and the gaseous products. A separation step then separates the gaseous products into hydrogen and off-gas.

Abstract translation: 描述了一种将含氧化合物进料在绝热固定床反应器中的催化剂上流动以产生反应器流出物和热量的方法。 绝热固定床反应器内的反应在约200℃至约375℃的反应温度下进行。 然后将反应器流出物冷凝以分离液体产物和气态产物。 然后分离步骤将气态产物分离成氢气和废气。

公开(公告)号：WO2019191113A1

公开(公告)日：2019-10-03

申请号：PCT/US2019/024095

申请日：2019-03-26

Applicant: PHILLIPS 66 COMPANY

Inventor： BALDRIDGE, Anthony O. ,  McDANIEL, Neal D. ,  SUTTIL, James, A. ,  KUNDU, Soumen ,  YAO, Jianhua ,  RANDOLPH, Bruce B. ,  SARDASHTI, Mazi ,  LUSK, Steven E. ,  WALTON, Robert, M.

IPC: C07C2/02 ,  C07C2/06 ,  C07C2/08 ,  C07C11/10

Abstract: The present disclosure relates generally to processes and systems that produce liquid transportation fuels by converting a hydrocarbon feed stream comprising both isopentane and n- pentane, and optionally, some C6+ hydrocarbons. Isopentane and smaller hydrocarbons are separated to form a first fraction while n-pentane and larger components of the feed stock form a second fraction. The first fraction is then catalytically-activated in a first reactor containing a first activation catalyst, while the second fraction is converted separately in a second reactor containing a second activation catalyst. The conditions maintained in each reactor are selected to maximize the conversion of each fraction to olefins and aromatics, while minimizing the production of C1-C4 light paraffins. In certain embodiments, the first fraction is activated at a lower temperature than the second fraction. Certain embodiments mix at least a portion of the effluents from the first and second activation zones and convert the resulting mixed effluent in either an oligomerization reactor containing an oligomerization catalyst or an oligomerization reactor containing an alkylation catalyst, thereby providing enhanced yields of upgraded hydrocarbon products that are characterized as a liquid transportation fuel or a blend component thereof.

公开(公告)号：EP2539274A1

公开(公告)日：2013-01-02

申请号：EP11748160.6

申请日：2011-02-25

Applicant: Phillips 66 Company

Inventor： HUGHES, Mark A. ,  LORD, Charles J. ,  RANDOLPH, Bruce B. ,  CROSS, Joe B. ,  KALAKKUNNATH, Sumod ,  CORBETT, Mike K. ,  GOENNER, Roger K. ,  REED, Larry E.

IPC: C01B19/00 ,  C02F1/62

CPC classification number: C02F1/58 ,  B01J20/0262 ,  B01J20/08 ,  B01J20/103 ,  B01J20/20 ,  B01J20/3204 ,  B01J20/3236 ,  C02F1/004 ,  C02F1/02 ,  C02F1/24 ,  C02F1/281 ,  C02F1/283 ,  C02F1/285 ,  C02F1/288 ,  C02F1/38 ,  C02F1/40 ,  C02F1/42 ,  C02F1/441 ,  C02F1/442 ,  C02F1/463 ,  C02F1/4693 ,  C02F1/5236 ,  C02F1/66 ,  C02F1/70 ,  C02F9/00 ,  C02F2001/007 ,  C02F2101/101 ,  C02F2101/103 ,  C02F2101/106 ,  C02F2101/20 ,  C02F2101/32 ,  C02F2101/325 ,  C02F2103/001 ,  C02F2103/10 ,  C02F2103/365 ,  C02F2301/08

Abstract: Methods and apparatus relate to treating fluid to at least reduce selenium content within the fluid. The treating includes conditioning stages to alter a composition of the fluid prior to removal of the selenium content from the fluid. The composition of the fluid after the conditioning stages facilitates the removal of the selenium content or at least limits detrimental impact to selenium removal efficiency.

公开(公告)号：EP3864115A1

公开(公告)日：2021-08-18

申请号：EP19871472.7

申请日：2019-10-04

Applicant: Phillips 66 Company

Inventor： BALDRIDGE, Anthony O. ,  McDANIEL, Neal D. ,  SUTTIL, James A. ,  WEINTROB, Edward C. ,  YAO, Jianhua ,  RANDOLPH, Bruce B. ,  SARDASHTI, Maziar ,  WALSTON, Robert M. ,  LUSK, Steven E.

IPC: C10G69/12 ,  C10G57/02 ,  C10G69/04

公开(公告)号：EP3774700A1

公开(公告)日：2021-02-17

申请号：EP19776158.8

申请日：2019-03-26

Applicant: Phillips 66 Company

Inventor： BALDRIDGE, Anthony O. ,  McDANIEL, Neal D. ,  SUTTIL, James A. ,  KUNDU, Soumen ,  YAO, Jianhua ,  RANDOLPH, Bruce B. ,  SARDASHTI, Mazi ,  LUSK, Steven E. ,  WALSTON, Jr., Robert M.

IPC: C07C2/02 ,  C07C2/06 ,  C07C2/08 ,  C07C11/10

公开(公告)号：EP2964569A1

公开(公告)日：2016-01-13

申请号：EP13855695.6

申请日：2013-11-11

Applicant: Phillips 66 Company ,  Paul, Uchenna P. ,  Randolph, Bruce B. ,  Nelson, Jon M. ,  Fjare, Kristi A. ,  Smith, Danielle K. ,  Cragun, Mark Rumel ,  Sadok, Richard, D.

Inventor： RANDOLPH, Bruce B. ,  FJARE, Kristi A. ,  SMITH, Danielle K. ,  CRAGUN, Mark Rumel ,  SADOK, Richard D.

IPC: C01B3/16

CPC classification number: C01B3/323 ,  C01B2203/0233 ,  C01B2203/0405 ,  C01B2203/0415 ,  C01B2203/043 ,  C01B2203/1041 ,  C01B2203/1058 ,  C01B2203/1076 ,  C01B2203/1082 ,  C01B2203/1094 ,  C01B2203/1211 ,  C01B2203/1217 ,  C01B2203/1223 ,  C01B2203/1229

Abstract: A process is described for flowing an oxygenate feed over a catalyst in an adiabatic fixed bed reactor to product a reactor effluent and heat. The reaction inside the adiabatic fixed bed reactor occurs at a reaction temperature from about 200
∘ C to about 375
∘ C. The reactor effluent is then condensed to separate the liquid products and the gaseous products. A separation step then separates the gaseous products into hydrogen and off-gas.

Abstract translation: 描述了一种将含氧化合物进料在绝热固定床反应器中的催化剂上流动以产生反应器流出物和热量的方法。 绝热固定床反应器中的反应在约200℃至约375℃的反应温度下进行。然后将反应器流出物冷凝以分离液体产物和气态产物。 分离步骤然后将气态产物分离成氢气和废气。