MXPA05013480A - Proceso hds mejorado usando corrientes de nafta seleccionadas. - Google Patents

Proceso hds mejorado usando corrientes de nafta seleccionadas.

Info

Publication number
MXPA05013480A
MXPA05013480A MXPA05013480A MXPA05013480A MXPA05013480A MX PA05013480 A MXPA05013480 A MX PA05013480A MX PA05013480 A MXPA05013480 A MX PA05013480A MX PA05013480 A MXPA05013480 A MX PA05013480A MX PA05013480 A MXPA05013480 A MX PA05013480A
Authority
MX
Mexico
Prior art keywords
boiling range
naphtha
range naphtha
light
mercaptans
Prior art date
Application number
MXPA05013480A
Other languages
English (en)
Inventor
Montri Vichailak
Original Assignee
Catalytic Distillation Tech
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 Catalytic Distillation Tech filed Critical Catalytic Distillation Tech
Publication of MXPA05013480A publication Critical patent/MXPA05013480A/es

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
    • C10G49/00—Treatment of hydrocarbon oils, in the presence of hydrogen or hydrogen-generating compounds, not provided for in a single one of groups C10G45/02, C10G45/32, C10G45/44, C10G45/58 or C10G47/00
    • C10G49/002—Apparatus for fixed bed hydrotreatment processes
    • 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
    • C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/40—Characteristics of the process deviating from typical ways of processing
    • C10G2300/4087—Catalytic distillation
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S203/00—Distillation: processes, separatory
    • Y10S203/06—Reactor-distillation

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)

Abstract

Un proceso para concurrentemente fraccionar e hidrotratar una corriente de nafta de gama completa. La corriente de nafta de gama de ebullicion completa se somete a la hidrodesulfuracion y separacion simultaneas en una nafta de gama de ebullicion ligera y una nafta de gama de ebullicion pesada, que se han tratado para convertir mercaptanos en las fracciones a H2S, que es separada con y separada de la nafta ligera que ademas es hidrodesulfurada al poner en contacto la nafta de gama de ebullicion ligera con hidrogeno en flujo a contracorriente en un lecho fijo de catalizador de hidrodesulfuracion para remover los mercaptanos recombinantes que se forman mediante la reaccion inversa de H2S con olefinas en la nafta durante la hidrodesulfuracion inicial, en donde la mejora comprende fraccionar la porcion de nafta de gama de ebullicion ligera para remover una fraccion mas ligera de la misma del reactor de flujo a contracorriente antes del contacto de la fraccion mas ligera con el catalizador de lecho fijo, debido a que la fraccion mas ligera esta sustancialmente libre de mercaptanos y no es beneficiada por el tratamiento adicional.
MXPA05013480A 2003-06-18 2004-05-05 Proceso hds mejorado usando corrientes de nafta seleccionadas. MXPA05013480A (es)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US10/463,959 US20040129606A1 (en) 2003-01-07 2003-06-18 HDS process using selected naphtha streams
PCT/US2004/013881 WO2005000996A2 (en) 2003-06-18 2004-05-05 Improved hds process using selected naphtha streams

Publications (1)

Publication Number Publication Date
MXPA05013480A true MXPA05013480A (es) 2006-03-09

Family

ID=33551384

Family Applications (1)

Application Number Title Priority Date Filing Date
MXPA05013480A MXPA05013480A (es) 2003-06-18 2004-05-05 Proceso hds mejorado usando corrientes de nafta seleccionadas.

Country Status (8)

Country Link
US (2) US20040129606A1 (es)
EP (1) EP1648980A2 (es)
CN (1) CN100368510C (es)
CA (1) CA2524353A1 (es)
MX (1) MXPA05013480A (es)
RU (1) RU2333934C2 (es)
WO (1) WO2005000996A2 (es)
ZA (1) ZA200509076B (es)

Families Citing this family (19)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20050035026A1 (en) * 2003-08-14 2005-02-17 Conocophillips Company Catalytic distillation hydroprocessing
MX2008014953A (es) 2006-05-26 2009-03-05 Bayer Healthcare Llc Combinaciones de medicamentos con diarilureas sustituidas para el tratamiento de cancer.
MX297306B (es) * 2006-11-22 2012-03-22 Ajinomoto Kk Procedimiento para la produccion de derivados de fenilalanina que tienen estructuras de base de quinazolinodiona e intermediarios para la produccion.
US8043495B2 (en) * 2008-01-25 2011-10-25 Catalytic Distillation Technologies Process to hydrodesulfurize FCC gasoline resulting in a low-mercaptan product
US8236172B2 (en) 2008-01-25 2012-08-07 Catalytic Distillation Technologies Process to hydrodesulfurize FCC gasoline resulting in a low-mercaptan product
EP2464620B1 (en) 2009-08-12 2013-10-02 Shell Internationale Research Maatschappij B.V. Process for removing an alkanol impurity from a dialkyl carbonate stream
US8628656B2 (en) 2010-08-25 2014-01-14 Catalytic Distillation Technologies Hydrodesulfurization process with selected liquid recycle to reduce formation of recombinant mercaptans
US20120074038A1 (en) * 2010-09-27 2012-03-29 Uop Llc Liquid phase hydroprocessing with low pressure drop
FR2993569B1 (fr) * 2012-07-17 2015-12-04 IFP Energies Nouvelles Procede de desulfuration d'une essence
FR3007416B1 (fr) * 2013-06-19 2018-03-23 IFP Energies Nouvelles Procede de production d'une essence a basse teneur en soufre et en mercaptans
FR3020376B1 (fr) * 2014-04-28 2017-10-20 Ifp Energies Now Procede de production d'une essence a basse temperature en soufre et en marcaptans.
EP2816094B1 (fr) 2013-06-19 2020-04-29 IFP Energies nouvelles Procédé de production d'une essence à basse teneur en soufre et en mercaptans
US9476000B2 (en) * 2013-07-10 2016-10-25 Uop Llc Hydrotreating process and apparatus
US10144883B2 (en) 2013-11-14 2018-12-04 Uop Llc Apparatuses and methods for desulfurization of naphtha
FR3014896B1 (fr) * 2013-12-18 2018-07-27 IFP Energies Nouvelles Procede d'hydrodesulfuration de coupes d'hydrocarbures
WO2016099787A1 (en) 2014-12-17 2016-06-23 Exxonmobil Chemical Patents Inc. Methods and systems for treating a hydrocarbon feed
RU2698100C2 (ru) * 2015-08-13 2019-08-22 Юоп Ллк Регулирование содержания меркаптанов при селективном гидрообессеривании нафты fcc
US10066174B2 (en) * 2016-03-22 2018-09-04 Uop Llc Process and apparatus for hydrotreating fractionated overhead naphtha
CN116059926B (zh) * 2021-10-29 2024-09-03 中国石油化工股份有限公司 加氢精馏反应器以及联合反应器

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Publication number Priority date Publication date Assignee Title
US4265735A (en) * 1979-12-21 1981-05-05 Mobil Oil Corporation ZSM-5 Zeolite catalyzes dialkyl disulfide conversion to hydrogen sulfide
CN1006710B (zh) * 1987-07-27 1990-02-07 上海化工厂 无尘复合铅盐稳定剂及其生产工艺
US5510089A (en) * 1991-07-22 1996-04-23 Chemical Research & Licensing Company Method for operating a distillation column reactor
US5169516A (en) * 1991-07-30 1992-12-08 Carr Norman L Removal of arsenic compounds from light hydrocarbon streams
US5320742A (en) * 1991-08-15 1994-06-14 Mobil Oil Corporation Gasoline upgrading process
JP3443474B2 (ja) 1995-02-03 2003-09-02 新日本石油株式会社 接触分解ガソリンの脱硫処理方法
US5659106A (en) * 1995-06-22 1997-08-19 Uop Catalytic distillation process for mercaptan and olefin removal
US5779883A (en) * 1995-07-10 1998-07-14 Catalytic Distillation Technologies Hydrodesulfurization process utilizing a distillation column realtor
US5597476A (en) * 1995-08-28 1997-01-28 Chemical Research & Licensing Company Gasoline desulfurization process
US5807477A (en) * 1996-09-23 1998-09-15 Catalytic Distillation Technologies Process for the treatment of light naphtha hydrocarbon streams
US5851383A (en) * 1997-01-09 1998-12-22 Uop Llc Process for thioetherification and selective hydrogenation of light olefins
US5759386A (en) * 1997-01-09 1998-06-02 Uop Process for thioetherification and selective hydrogenation of light hydrocarbons
US6083378A (en) * 1998-09-10 2000-07-04 Catalytic Distillation Technologies Process for the simultaneous treatment and fractionation of light naphtha hydrocarbon streams
US6231752B1 (en) * 1999-09-17 2001-05-15 Catalytic Distillation Technologies Process for the removal of mercaptans
US6495030B1 (en) * 2000-10-03 2002-12-17 Catalytic Distillation Technologies Process for the desulfurization of FCC naphtha
US6416658B1 (en) * 2000-10-19 2002-07-09 Catalytic Distillation Technologies Process for simultaneous hydrotreating and splitting of naphtha streams
US6444118B1 (en) * 2001-02-16 2002-09-03 Catalytic Distillation Technologies Process for sulfur reduction in naphtha streams
CN1141363C (zh) * 2001-04-28 2004-03-10 中国石油化工股份有限公司 一种轻质油品选择性脱硫醇的方法

Also Published As

Publication number Publication date
US20040129606A1 (en) 2004-07-08
WO2005000996A2 (en) 2005-01-06
CN1809624A (zh) 2006-07-26
ZA200509076B (en) 2007-09-26
EP1648980A2 (en) 2006-04-26
RU2006101327A (ru) 2006-05-27
WO2005000996A3 (en) 2005-05-19
RU2333934C2 (ru) 2008-09-20
CA2524353A1 (en) 2005-01-06
CN100368510C (zh) 2008-02-13
US7291258B2 (en) 2007-11-06
US20060065578A1 (en) 2006-03-30

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