ES2191592T3 - Procedimiento de hidrocraqueo mejorado. - Google Patents

Procedimiento de hidrocraqueo mejorado.

Info

Publication number
ES2191592T3
ES2191592T3 ES00125533T ES00125533T ES2191592T3 ES 2191592 T3 ES2191592 T3 ES 2191592T3 ES 00125533 T ES00125533 T ES 00125533T ES 00125533 T ES00125533 T ES 00125533T ES 2191592 T3 ES2191592 T3 ES 2191592T3
Authority
ES
Spain
Prior art keywords
stream
hydrocarbonaceous
hydrogen
zone
liquid
Prior art date
Legal status (The legal status 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 status listed.)
Expired - Lifetime
Application number
ES00125533T
Other languages
English (en)
Inventor
Tom N Kalnes
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Honeywell UOP LLC
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
Application granted granted Critical
Publication of ES2191592T3 publication Critical patent/ES2191592T3/es
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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
    • 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
    • C10G69/04—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 catalytic cracking in the absence of hydrogen
    • 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
    • C10G65/02—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only
    • C10G65/12—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only including cracking steps and other hydrotreatment steps
    • 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
    • C10G49/22—Separation of effluents

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)
  • Catalysts (AREA)
  • Yarns And Mechanical Finishing Of Yarns Or Ropes (AREA)
  • Inspection Of Paper Currency And Valuable Securities (AREA)
  • Diaphragms For Electromechanical Transducers (AREA)

Abstract

Un procedimiento para hidrocraquear una materia prima hidrocarbonada, procedimiento que comprende: (a) Pasar una materia prima hidrocarbonada, una corriente líquida de reciclo e hidrógeno por una zona de reacción de desnitrificación y desulfuración que contiene un catalizador y recuperar de la misma un efluente de la zona de reacción de desnitrificación y desulfuración; (b) Pasar dicho efluente de la zona de reacción de desnitrificación y desulfuración por una zona de hidrocraqueo que contiene un catalizador de hidrocraqueo; (c) Pasar el efluente resultante de dicha zona de hidrocraqueo directamente a un equipo de extracción caliente a alta presión utilizando un gas de extracción caliente rico en hidrógeno, para producir una primera corriente de vapor que comprende hidrógeno, compuestos hidrocarbonados que tienen un punto de ebullición con una temperatura por debajo del intervalo de ebullición de dicha materia prima hidrocarbonada, sulfuro de hidrógeno y amoníaco, y una primera corriente líquida que comprende compuestos hidrocarbonados que tienen un punto de ebullición en el intervalo de dicha materia prima hidrocarbonada; (d) Pasar por dicha zona de reacción de desnitrificación y desulfuración al menos una porción de dicha primera corriente líquida, que comprende compuestos hidrocarbonados que tienen un punto de ebullición en el intervalo de dicha materia prima hidrocarbonada, como al menos una porción de dicha corriente líquida; (e) Pasar al menos una porción de dicha primera corriente de vapor de la etapa (c) que comprende hidrógeno y compuestos hidrocarbonados, por una zona de saturación de compuestos aromáticos, para reducir la concentración de compuestos aromáticos; y (f) Pasar y enfriar el efluente resultante de dicha zona de saturación de compuestos aromáticos de la etapa (e) y al menos una porción de dicha primera corriente líquida de la etapa (c) por un separador líquido-vapor, para producir una corriente gaseosa rica en hidrógeno y una corriente de productos hidrocarbonados hidrocraqueados.
ES00125533T 1999-11-23 2000-11-22 Procedimiento de hidrocraqueo mejorado. Expired - Lifetime ES2191592T3 (es)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US09/447,247 US6402935B1 (en) 1999-11-23 1999-11-23 Hydrocracking process

Publications (1)

Publication Number Publication Date
ES2191592T3 true ES2191592T3 (es) 2003-09-16

Family

ID=23775573

Family Applications (1)

Application Number Title Priority Date Filing Date
ES00125533T Expired - Lifetime ES2191592T3 (es) 1999-11-23 2000-11-22 Procedimiento de hidrocraqueo mejorado.

Country Status (9)

Country Link
US (1) US6402935B1 (es)
EP (1) EP1103592B1 (es)
KR (1) KR100776932B1 (es)
AT (1) ATE232232T1 (es)
AU (1) AU774809B2 (es)
CA (1) CA2326310C (es)
DE (1) DE60001349T2 (es)
ES (1) ES2191592T3 (es)
ID (1) ID28426A (es)

Families Citing this family (29)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6328879B1 (en) * 1999-07-26 2001-12-11 Uop Llc Simultaneous hydroprocesssing of two feedstocks
US6703149B2 (en) * 2000-12-20 2004-03-09 Masaya Kuno Method and apparatus for producing reformed hydrocarbon and hydrogen, engine installed with fuel cell, and energy station
AU783493B2 (en) * 2001-06-20 2005-11-03 Uop Llc Simultaneous hydroprocessing of two feedstocks
US6623623B2 (en) * 2001-06-28 2003-09-23 Uop Llc Simultaneous hydroprocessing of two feedstocks
DE602005013215D1 (de) * 2005-08-09 2009-04-23 Uop Llc Hydrokrackverfahren zum Erzeugen von Diesel mit extrem niedrigem Schwefelgehalt
CN1912064B (zh) * 2005-08-11 2010-12-29 环球油品公司 生产超低硫柴油的加氢裂化方法
RU2386669C2 (ru) * 2005-09-02 2010-04-20 Юоп Ллк Способ каталитического гидрокрекинга углеводородного сырья для получения сверхмалосернистого дизельного топлива
US7906013B2 (en) 2006-12-29 2011-03-15 Uop Llc Hydrocarbon conversion process
US7794585B2 (en) * 2007-10-15 2010-09-14 Uop Llc Hydrocarbon conversion process
US8575409B2 (en) 2007-12-20 2013-11-05 Syntroleum Corporation Method for the removal of phosphorus
US8581013B2 (en) 2008-06-04 2013-11-12 Syntroleum Corporation Biorenewable naphtha composition and methods of making same
US20090300971A1 (en) 2008-06-04 2009-12-10 Ramin Abhari Biorenewable naphtha
US8008534B2 (en) * 2008-06-30 2011-08-30 Uop Llc Liquid phase hydroprocessing with temperature management
US8999141B2 (en) * 2008-06-30 2015-04-07 Uop Llc Three-phase hydroprocessing without a recycle gas compressor
US9279087B2 (en) * 2008-06-30 2016-03-08 Uop Llc Multi-staged hydroprocessing process and system
KR101111006B1 (ko) * 2008-08-14 2012-02-15 에스케이에너지 주식회사 석유계 탄화수소 탈황 공정의 수소 회수 방법 및 장치
US8231804B2 (en) 2008-12-10 2012-07-31 Syntroleum Corporation Even carbon number paraffin composition and method of manufacturing same
US8221706B2 (en) * 2009-06-30 2012-07-17 Uop Llc Apparatus for multi-staged hydroprocessing
US8518241B2 (en) * 2009-06-30 2013-08-27 Uop Llc Method for multi-staged hydroprocessing
US8529754B2 (en) * 2009-09-28 2013-09-10 China Petroleum & Chemical Corporation Catalytic conversion process for producing more diesel and propylene
US8894839B2 (en) * 2010-02-22 2014-11-25 Uop Llc Process, system, and apparatus for a hydrocracking zone
US8394900B2 (en) 2010-03-18 2013-03-12 Syntroleum Corporation Profitable method for carbon capture and storage
CN102703109A (zh) * 2012-05-30 2012-10-03 中国石油集团工程设计有限责任公司北京分公司 一种气提法从原油中脱除硫的方法
US9157038B2 (en) 2012-09-28 2015-10-13 Uop Llc Process for washing a gas from a hydroprocessed effluent, and an apparatus and separator relating thereto
US9328303B2 (en) 2013-03-13 2016-05-03 Reg Synthetic Fuels, Llc Reducing pressure drop buildup in bio-oil hydroprocessing reactors
US8969259B2 (en) 2013-04-05 2015-03-03 Reg Synthetic Fuels, Llc Bio-based synthetic fluids
US9687808B2 (en) 2013-07-26 2017-06-27 Shell Oil Company Method and system for controlling a hydrocracker and fractionator
CN105838418B (zh) * 2016-06-13 2017-05-31 黑龙江省能源环境研究院 一种提高页岩油加氢精制脱氮率的方法
CN106202651B (zh) * 2016-06-25 2019-03-01 山东交通学院 一种热再生沥青混合料矿料级配的优化设计方法

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Publication number Priority date Publication date Assignee Title
US3159564A (en) * 1961-10-20 1964-12-01 Union Oil Co Integral hydrofining-hydro-cracking process
US3328290A (en) 1965-03-30 1967-06-27 Standard Oil Co Two-stage process for the hydrocracking of hydrocarbon oils in which the feed oil ispretreated in the first stage
US3256178A (en) * 1965-05-25 1966-06-14 Union Oil Co Hydrocracking process
US3592757A (en) * 1969-03-17 1971-07-13 Union Oil Co Combination hydrocracking-hydrogenation process
US4435275A (en) * 1982-05-05 1984-03-06 Mobil Oil Corporation Hydrocracking process for aromatics production
FR2600669B1 (fr) * 1986-06-27 1989-04-07 Inst Francais Du Petrole Procede d'hydrocraquage destine a la production de distillats moyens
US5110444A (en) * 1990-08-03 1992-05-05 Uop Multi-stage hydrodesulfurization and hydrogenation process for distillate hydrocarbons
US5114562A (en) 1990-08-03 1992-05-19 Uop Two-stage hydrodesulfurization and hydrogenation process for distillate hydrocarbons
JP2001523277A (ja) 1996-04-09 2001-11-20 シェブロン ユー．エス．エー．インコーポレイテッド ハイドロプロセシング反応器系の逆順操作法
US6153086A (en) * 1996-08-23 2000-11-28 Exxon Research And Engineering Company Combination cocurrent and countercurrent staged hydroprocessing with a vapor stage
US5720872A (en) 1996-12-31 1998-02-24 Exxon Research And Engineering Company Multi-stage hydroprocessing with multi-stage stripping in a single stripper vessel
US5980729A (en) * 1998-09-29 1999-11-09 Uop Llc Hydrocracking process
US6190535B1 (en) * 1999-08-20 2001-02-20 Uop Llc Hydrocracking process

Also Published As

Publication number Publication date
KR100776932B1 (ko) 2007-11-20
EP1103592A2 (en) 2001-05-30
EP1103592A3 (en) 2002-02-06
EP1103592B1 (en) 2003-02-05
CA2326310C (en) 2009-11-10
ATE232232T1 (de) 2003-02-15
US6402935B1 (en) 2002-06-11
AU7176800A (en) 2001-05-24
KR20010088296A (ko) 2001-09-26
DE60001349T2 (de) 2003-12-24
CA2326310A1 (en) 2001-05-23
ID28426A (id) 2001-05-24
AU774809B2 (en) 2004-07-08
DE60001349D1 (de) 2003-03-13

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