SG11201401163TA - Integrated hydrogenation/dehydrogenation reactor in a catalytic reforming process configuration for improved aromatics production - Google Patents

Integrated hydrogenation/dehydrogenation reactor in a catalytic reforming process configuration for improved aromatics production

Info

Publication number
SG11201401163TA
SG11201401163TA SG11201401163TA SG11201401163TA SG11201401163TA SG 11201401163T A SG11201401163T A SG 11201401163TA SG 11201401163T A SG11201401163T A SG 11201401163TA SG 11201401163T A SG11201401163T A SG 11201401163TA SG 11201401163T A SG11201401163T A SG 11201401163TA
Authority
SG
Singapore
Prior art keywords
reforming process
catalytic reforming
process configuration
dehydrogenation reactor
aromatics production
Prior art date
Application number
SG11201401163TA
Inventor
Manuela Serban
Bussche Kurt M Vanden
Mark D Moser
David A Wegerer
Original Assignee
Uop Llc
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Uop Llc filed Critical Uop Llc
Publication of SG11201401163TA publication Critical patent/SG11201401163TA/en

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G59/00—Treatment of naphtha by two or more reforming processes only or by at least one reforming process and at least one process which does not substantially change the boiling range of the naphtha
    • C10G59/02—Treatment of naphtha by two or more reforming processes only or by at least one reforming process and at least one process which does not substantially change the boiling range of the naphtha plural serial stages only
    • C10G59/04—Treatment of naphtha by two or more reforming processes only or by at least one reforming process and at least one process which does not substantially change the boiling range of the naphtha plural serial stages only including at least one catalytic and at least one non-catalytic reforming step
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G69/00—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one other conversion process
    • C10G69/02—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one other conversion process plural serial stages only
    • C10G69/08—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one other conversion process plural serial stages only including at least one step of reforming naphtha
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G2400/00—Products obtained by processes covered by groups C10G9/00 - C10G69/14
    • C10G2400/30—Aromatics

Landscapes

  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Catalysts (AREA)
SG11201401163TA 2011-12-15 2012-09-14 Integrated hydrogenation/dehydrogenation reactor in a catalytic reforming process configuration for improved aromatics production SG11201401163TA (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US13/327,170 US9528051B2 (en) 2011-12-15 2011-12-15 Integrated hydrogenation/dehydrogenation reactor in a catalytic reforming process configuration for improved aromatics production
PCT/US2012/055267 WO2013089856A1 (en) 2011-12-15 2012-09-14 Integrated hydrogenation/dehydrogenation reactor in a catalytic reforming process configuration for improved aromatics production

Publications (1)

Publication Number Publication Date
SG11201401163TA true SG11201401163TA (en) 2014-04-28

Family

ID=48610788

Family Applications (1)

Application Number Title Priority Date Filing Date
SG11201401163TA SG11201401163TA (en) 2011-12-15 2012-09-14 Integrated hydrogenation/dehydrogenation reactor in a catalytic reforming process configuration for improved aromatics production

Country Status (7)

Country Link
US (1) US9528051B2 (en)
CN (1) CN103857646A (en)
BR (1) BR112014007976A2 (en)
MY (1) MY162522A (en)
RU (1) RU2014113320A (en)
SG (1) SG11201401163TA (en)
WO (1) WO2013089856A1 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104672048B (en) * 2015-02-11 2016-06-08 辽宁省盘锦监狱 A kind of method preparing butadiene and hexamethylene

Family Cites Families (25)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3392107A (en) * 1966-01-05 1968-07-09 Sinclair Research Inc Process for reforming naphthene and paraffin containing hydrocarbons in the naphtha boiling point range in several stages to obtain a high octane gasoline
US3753891A (en) 1971-01-15 1973-08-21 R Graven Split-stream reforming to upgrade low-octane hydrocarbons
US4839024A (en) 1987-09-10 1989-06-13 Mobil Oil Corporation Split-feed naphtha reforming process
US4914075A (en) 1988-12-05 1990-04-03 Uop Dehydrogenation catalyst composition
US5242576A (en) 1991-11-21 1993-09-07 Uop Selective upgrading of naphtha fractions by a combination of reforming and selective isoparaffin synthesis
RU3225U1 (en) 1994-09-16 1996-12-16 Товарищество с ограниченной ответственностью - Научно-производственное объединение "Ленар" REACTOR-REGENERATION UNIT FOR INSTALLING THE CATALYTIC CONVERSION OF HYDROCARBONS
US5683573A (en) 1994-12-22 1997-11-04 Uop Continuous catalytic reforming process with dual zones
US5935415A (en) * 1994-12-22 1999-08-10 Uop Llc Continuous catalytic reforming process with dual zones
CN1108353C (en) * 1997-11-03 2003-05-14 环球油品公司 Continuous catalytic reforming combined with zeolitic reforming for increased BTX yield
US6004452A (en) * 1997-11-14 1999-12-21 Chevron Chemical Company Llc Process for converting hydrocarbon feed to high purity benzene and high purity paraxylene
US6900365B2 (en) 1999-11-15 2005-05-31 Chevron Phillips Chemical Company Lp Process for converting heavy hydrocarbon feeds to high octane gasoline, BTX and other valuable aromatics
US7288687B1 (en) 2006-05-18 2007-10-30 Uop Llc Integrated process for aromatics production
US7553998B2 (en) * 2006-06-21 2009-06-30 Uop Llc Energy-efficient process for para-xylene production
US8679321B2 (en) 2011-04-29 2014-03-25 Uop Llc Process for increasing benzene and toluene production
US9102881B2 (en) 2011-04-29 2015-08-11 Uop Llc Process for increasing aromatics production from naphtha
US8680351B2 (en) 2011-04-29 2014-03-25 Uop Llc Process for increasing benzene and toluene production
US8845883B2 (en) 2011-04-29 2014-09-30 Uop Llc Process for increasing aromatics production
US8926829B2 (en) 2011-04-29 2015-01-06 Uop Llc Process for increasing benzene and toluene production
US8604262B2 (en) 2011-04-29 2013-12-10 Uop Llc Process for increasing aromatics production
US8906226B2 (en) 2011-04-29 2014-12-09 Uop Llc Process for increasing aromatics production
US9023298B2 (en) 2011-04-29 2015-05-05 Uop Llc High temperature platformer
US8679320B2 (en) 2011-04-29 2014-03-25 Uop Llc Process for increasing benzene and toluene production
US8845884B2 (en) 2011-04-29 2014-09-30 Uop Llc Process for increasing aromatics production
US20120277500A1 (en) 2011-04-29 2012-11-01 Uop Llc High Temperature Platforming Process
US20120277511A1 (en) 2011-04-29 2012-11-01 Uop Llc High Temperature Platformer

Also Published As

Publication number Publication date
BR112014007976A2 (en) 2017-04-11
MY162522A (en) 2017-06-15
US9528051B2 (en) 2016-12-27
CN103857646A (en) 2014-06-11
US20130158310A1 (en) 2013-06-20
WO2013089856A1 (en) 2013-06-20
RU2014113320A (en) 2015-10-10

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