[go: up one dir, main page]

SG83703A1 - Process using staggered bypassing of reaction zones for increased capacity - Google Patents

Process using staggered bypassing of reaction zones for increased capacity

Info

Publication number
SG83703A1
SG83703A1 SG9901060A SG1999001060A SG83703A1 SG 83703 A1 SG83703 A1 SG 83703A1 SG 9901060 A SG9901060 A SG 9901060A SG 1999001060 A SG1999001060 A SG 1999001060A SG 83703 A1 SG83703 A1 SG 83703A1
Authority
SG
Singapore
Prior art keywords
zone
reaction
reaction zones
reaction zone
effluent stream
Prior art date
Application number
SG9901060A
Other languages
English (en)
Inventor
D Peters Kenneth
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
Priority to US08/704,224 priority Critical patent/US5879537A/en
Priority to AU18576/99A priority patent/AU767083B2/en
Priority to DE69932314T priority patent/DE69932314T2/de
Priority to AT99301627T priority patent/ATE332952T1/de
Priority to CA002264498A priority patent/CA2264498C/en
Priority to PT99301627T priority patent/PT1033398E/pt
Priority to EP99301627A priority patent/EP1033398B1/de
Priority to ES99301627T priority patent/ES2268829T3/es
Application filed by Uop Llc filed Critical Uop Llc
Priority to SG9901060A priority patent/SG83703A1/en
Priority to RU99104506/04A priority patent/RU2208623C2/ru
Priority to JP05887999A priority patent/JP4018835B2/ja
Priority to TW088103462A priority patent/TW499473B/zh
Priority to ZA9901838A priority patent/ZA991838B/xx
Priority to CNB991032128A priority patent/CN1200914C/zh
Publication of SG83703A1 publication Critical patent/SG83703A1/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
    • C10G65/00—Treatment of hydrocarbon oils by two or more hydrotreatment processes only
    • 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
    • C10G51/00—Treatment of hydrocarbon oils, in the absence of hydrogen, by two or more cracking processes only
    • 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

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)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Battery Electrode And Active Subsutance (AREA)
  • Superconductors And Manufacturing Methods Therefor (AREA)
  • Steroid Compounds (AREA)
  • Signal Processing For Digital Recording And Reproducing (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
SG9901060A 1996-08-23 1999-03-05 Process using staggered bypassing of reaction zones for increased capacity SG83703A1 (en)

Priority Applications (14)

Application Number Priority Date Filing Date Title
US08/704,224 US5879537A (en) 1996-08-23 1996-08-23 Hydrocarbon conversion process using staggered bypassing of reaction zones
AU18576/99A AU767083B2 (en) 1996-08-23 1999-03-03 Process using staggered bypassing of reaction zones for increased capacity
AT99301627T ATE332952T1 (de) 1996-08-23 1999-03-04 Verfahren mit erhöhter kapazität unter verwendung einer gestaffelten umführung von rektionstufen
CA002264498A CA2264498C (en) 1996-08-23 1999-03-04 Process using staggered bypassing of reaction zones for increased capacity
PT99301627T PT1033398E (pt) 1996-08-23 1999-03-04 Processo que utiliza o desvio escalonado de zonas de reaccao para aumento da capacidade
EP99301627A EP1033398B1 (de) 1996-08-23 1999-03-04 Verfahren mit erhöhter Kapazität unter Verwendung einer gestaffelten Umführung von Rektionstufen
ES99301627T ES2268829T3 (es) 1996-08-23 1999-03-04 Procedimiento que emplea una desviacion escalonada de las zonas de reaccion para un aumento de capacidad.
DE69932314T DE69932314T2 (de) 1996-08-23 1999-03-04 Verfahren mit erhöhter Kapazität unter Verwendung einer gestaffelten Umführung von Rektionstufen
SG9901060A SG83703A1 (en) 1996-08-23 1999-03-05 Process using staggered bypassing of reaction zones for increased capacity
RU99104506/04A RU2208623C2 (ru) 1996-08-23 1999-03-05 Способ конверсии углеводородов
JP05887999A JP4018835B2 (ja) 1996-08-23 1999-03-05 処理能力向上のために反応ゾーンのジグザグ・バイパスを用いる方法
TW088103462A TW499473B (en) 1996-08-23 1999-03-06 Process using staggered bypassing of reaction zones for increased capacity
ZA9901838A ZA991838B (en) 1996-08-23 1999-03-08 Process using staggered bypassing of reaction zones for increased capacity.
CNB991032128A CN1200914C (zh) 1996-08-23 1999-03-09 采用反应区错列旁路以提高生产能力的方法

Applications Claiming Priority (9)

Application Number Priority Date Filing Date Title
US08/704,224 US5879537A (en) 1996-08-23 1996-08-23 Hydrocarbon conversion process using staggered bypassing of reaction zones
AU18576/99A AU767083B2 (en) 1996-08-23 1999-03-03 Process using staggered bypassing of reaction zones for increased capacity
EP99301627A EP1033398B1 (de) 1996-08-23 1999-03-04 Verfahren mit erhöhter Kapazität unter Verwendung einer gestaffelten Umführung von Rektionstufen
CA002264498A CA2264498C (en) 1996-08-23 1999-03-04 Process using staggered bypassing of reaction zones for increased capacity
RU99104506/04A RU2208623C2 (ru) 1996-08-23 1999-03-05 Способ конверсии углеводородов
SG9901060A SG83703A1 (en) 1996-08-23 1999-03-05 Process using staggered bypassing of reaction zones for increased capacity
JP05887999A JP4018835B2 (ja) 1996-08-23 1999-03-05 処理能力向上のために反応ゾーンのジグザグ・バイパスを用いる方法
ZA9901838A ZA991838B (en) 1996-08-23 1999-03-08 Process using staggered bypassing of reaction zones for increased capacity.
CNB991032128A CN1200914C (zh) 1996-08-23 1999-03-09 采用反应区错列旁路以提高生产能力的方法

Publications (1)

Publication Number Publication Date
SG83703A1 true SG83703A1 (en) 2001-10-16

Family

ID=32111205

Family Applications (1)

Application Number Title Priority Date Filing Date
SG9901060A SG83703A1 (en) 1996-08-23 1999-03-05 Process using staggered bypassing of reaction zones for increased capacity

Country Status (14)

Country Link
US (1) US5879537A (de)
EP (1) EP1033398B1 (de)
JP (1) JP4018835B2 (de)
CN (1) CN1200914C (de)
AT (1) ATE332952T1 (de)
AU (1) AU767083B2 (de)
CA (1) CA2264498C (de)
DE (1) DE69932314T2 (de)
ES (1) ES2268829T3 (de)
PT (1) PT1033398E (de)
RU (1) RU2208623C2 (de)
SG (1) SG83703A1 (de)
TW (1) TW499473B (de)
ZA (1) ZA991838B (de)

Families Citing this family (30)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5879537A (en) * 1996-08-23 1999-03-09 Uop Llc Hydrocarbon conversion process using staggered bypassing of reaction zones
US7351325B2 (en) * 2003-07-18 2008-04-01 Saudi Arabian Oil Company Catalytic naphtha reforming process
US7569085B2 (en) * 2004-12-27 2009-08-04 General Electric Company System and method for hydrogen production
US7740751B2 (en) 2006-11-09 2010-06-22 Uop Llc Process for heating a stream for a hydrocarbon conversion process
US20080110801A1 (en) * 2006-11-09 2008-05-15 Leon Yuan Process For Heating A Hydrocarbon Stream Entering A Reaction Zone With A Heater Convection Section
US20080141860A1 (en) * 2006-12-18 2008-06-19 Morgan Edward R Process for increasing hydrogen recovery
US7622620B2 (en) * 2006-12-22 2009-11-24 Uop Llc Hydrocarbon conversion process including a staggered-bypass reaction system
DE102007059243A1 (de) * 2007-12-07 2009-06-10 Uhde Gmbh Verfahren zur Entschwefelung olefinhaltiger Einsatzstoffe
US7909988B2 (en) * 2008-04-17 2011-03-22 Uop Llc Process and system for the transfer of a metal catalyst component from one particle to another
US20100116714A1 (en) * 2008-11-12 2010-05-13 Lapinski Mark P Process and System for the Addition of Promoter Metal In Situ in a Catalytic Reforming Unit
US7799729B2 (en) * 2009-02-23 2010-09-21 Uop Llc Reforming catalyst
RU2505516C2 (ru) * 2009-03-05 2014-01-27 Юоп Ллк Способ дегидрирования углеводородов
US8282814B2 (en) * 2009-03-31 2012-10-09 Uop Llc Fired heater for a hydrocarbon conversion process
CN102071054B (zh) * 2009-10-30 2013-07-31 中国石油化工股份有限公司 一种催化裂化方法
US8329028B2 (en) * 2009-12-17 2012-12-11 Uop Llc Solid catalyst hydrocarbon conversion process using stacked moving bed reactors
US9023298B2 (en) * 2011-04-29 2015-05-05 Uop Llc High temperature platformer
US8608941B2 (en) * 2011-10-07 2013-12-17 Uop Llc Reforming process with integrated fluid catalytic cracker gasoline and hydroprocessed cycle oil
US9024099B2 (en) * 2011-12-15 2015-05-05 Uop Llc Co-current catalyst flow with feed for fractionated feed recombined and sent to high temperature reforming reactors
US8912110B2 (en) 2012-03-29 2014-12-16 Uop Llc Catalyst for conversion of hydrocarbons
US9266091B2 (en) 2012-03-29 2016-02-23 Uop Llc Reforming catalysts with tuned acidity for maximum aromatics yield
US8900442B2 (en) 2012-11-20 2014-12-02 Uop Llc High temperature CCR process with integrated reactor bypasses
US9206358B2 (en) 2013-03-29 2015-12-08 Uop Llc Methods and apparatuses for heating hydrocarbon streams for processing
CN105462608B (zh) * 2014-09-12 2017-06-30 中国石油化工股份有限公司 一种石脑油连续催化重整方法
CN106590743B (zh) * 2015-10-20 2018-07-31 中国石油化工股份有限公司 一种生产润滑油基础油的方法
CN106590737B (zh) * 2015-10-20 2018-07-31 中国石油化工股份有限公司 一种加工高芳烃劣质原料油的方法
CN108699448A (zh) 2016-05-13 2018-10-23 环球油品公司 改进了加热器集成的重整方法
US10336666B2 (en) 2017-08-09 2019-07-02 Uop Llc Processes for producing olefins from paraffins
US10865350B2 (en) * 2017-09-30 2020-12-15 Uop Llc Process for hydroprocessing a hydrocarbon stream
WO2019210239A1 (en) 2018-04-26 2019-10-31 Uop Llc Process and apparatus for a convection charge heater
CA3118248A1 (en) * 2018-10-29 2020-05-07 China Petroleum & Chemical Corporation A liquid-solid radial moving bed reaction apparatus and a solid acid alkylation process

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4250019A (en) * 1979-09-06 1981-02-10 Uop Inc. Multiple stage hydrocarbon conversion process
US4325807A (en) * 1981-01-05 1982-04-20 Uop Inc. Multiple stage hydrocarbon conversion with gravity flowing catalyst particles
US5879537A (en) * 1996-08-23 1999-03-09 Uop Llc Hydrocarbon conversion process using staggered bypassing of reaction zones

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3657110A (en) * 1970-01-05 1972-04-18 Standard Oil Co Process for hydrocracking nitrogen-containing feedstocks
US4119526A (en) * 1977-05-09 1978-10-10 Uop Inc. Multiple-stage hydrocarbon conversion with gravity-flowing catalyst particles
US4325806A (en) * 1981-01-05 1982-04-20 Uop Inc. Multiple stage hydrocarbon conversion with gravity flowing catalyst particles

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4250019A (en) * 1979-09-06 1981-02-10 Uop Inc. Multiple stage hydrocarbon conversion process
US4325807A (en) * 1981-01-05 1982-04-20 Uop Inc. Multiple stage hydrocarbon conversion with gravity flowing catalyst particles
US5879537A (en) * 1996-08-23 1999-03-09 Uop Llc Hydrocarbon conversion process using staggered bypassing of reaction zones

Also Published As

Publication number Publication date
CA2264498A1 (en) 2000-09-04
US5879537A (en) 1999-03-09
TW499473B (en) 2002-08-21
CN1266038A (zh) 2000-09-13
JP2000256673A (ja) 2000-09-19
EP1033398B1 (de) 2006-07-12
ATE332952T1 (de) 2006-08-15
RU2208623C2 (ru) 2003-07-20
CA2264498C (en) 2009-09-22
AU767083B2 (en) 2003-10-30
EP1033398A1 (de) 2000-09-06
DE69932314D1 (de) 2006-08-24
CN1200914C (zh) 2005-05-11
ZA991838B (en) 2000-01-26
ES2268829T3 (es) 2007-03-16
PT1033398E (pt) 2006-09-29
AU1857699A (en) 2000-09-07
JP4018835B2 (ja) 2007-12-05
DE69932314T2 (de) 2007-07-05

Similar Documents

Publication Publication Date Title
SG83703A1 (en) Process using staggered bypassing of reaction zones for increased capacity
ES477157A1 (es) Un procedimiento de preparacion de una composicion cataliti-ca acida sulfurada selectivamente.
RU99104506A (ru) Способ конверсии углеводородов
WO2002100808A3 (en) Continuous process for the alkylation of hydrocarbons
EP1287882A3 (de) Verfahren zum Screening einer Katalysatorbibliothek
CA2235491A1 (en) Method based on a fluidized-bed reactor for converting hydrocarbons
IL131394A0 (en) Chromatographic purification of chlorinated sucrose
TW357104B (en) Perfluorocompound separation and purification method and system
CA2447095A1 (en) Methods for reducing entrainment of solids and liquids
ES8107039A1 (es) Un sistema de separacion de gas y solidos para separar una corriente diluida de fase mixta de gas y solidos en parti- culas
AU726453B2 (en) Method for biological purification of waste water by the activated sludge method and apparatus for carrying out the method
GB1307782A (en) Staged regeneration of catalyst
RU2210566C2 (ru) Способ выделения олефинненасыщенных нитрилов
EP0905216A3 (de) Gegenstromreaktor mit zwischenstufiger Entfernung in Gas-Flüssigkeit Kontaktzonen
ES8300842A1 (es) "metodo de efectuar la conversion de un material de carga hidrocarbonado".
EP0751121A3 (de) Verfahren zur Herstellung von Harnstoff in zwei separaten Reaktionszonen
MY126576A (en) Alternated process for olefin metathesis.
UA32509C2 (uk) Спосіб екзотермічного гетерогенного синтезу і реактор для його здійснення
CN1033749C (zh) 生产环酐的方法
MY117359A (en) Improved acrylonitrile recovery process
CA2096438A1 (en) Hydrocyclone plant
EP0776686B1 (de) Vielstufige Gas/Feststofftrennvorrichtung und Verfahren
US20040042946A1 (en) Method and installation for purifying cement plant fumes
MXPA99002288A (es) Proceso usando derivacion salteada de zonas de reaccion para capacidad incrementada.
FR2801605B1 (fr) Procede et dispositif pour la production d'aromatiques incluant une reduction du catalyseur