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PE20001200A1 - Proceso para mejorar el petroleo crudo usando hidrogeno - Google Patents

Proceso para mejorar el petroleo crudo usando hidrogeno

Info

Publication number
PE20001200A1
PE20001200A1 PE1999000980A PE00098099A PE20001200A1 PE 20001200 A1 PE20001200 A1 PE 20001200A1 PE 1999000980 A PE1999000980 A PE 1999000980A PE 00098099 A PE00098099 A PE 00098099A PE 20001200 A1 PE20001200 A1 PE 20001200A1
Authority
PE
Peru
Prior art keywords
hydrogen
primary tank
current
crude oil
cuts
Prior art date
Application number
PE1999000980A
Other languages
English (en)
Inventor
Robert Satchwell
Jose Lourenco
Patrick J Cochrane
Roderick M Facey
Joao Rodrigues
Kenneth Bannard
Hannu Salokangas
Original Assignee
Canadian Environmental Inc
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 Canadian Environmental Inc filed Critical Canadian Environmental Inc
Publication of PE20001200A1 publication Critical patent/PE20001200A1/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
    • C10G45/00—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
    • C10G45/58—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to change the structural skeleton of some of the hydrocarbon content without cracking the other hydrocarbons present, e.g. lowering pour point; Selective hydrocracking of normal paraffins
    • 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
    • C10G45/00—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
    • 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
    • C10G45/00—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
    • C10G45/02—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing
    • C10G45/22—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing with hydrogen dissolved or suspended in the oil
    • 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
    • C10G47/00—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions
    • 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
    • C10G49/007—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 in the presence of hydrogen from a special source or of a special composition or having been purified by a special treatment

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)
  • Crystallography & Structural Chemistry (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Abstract

EL CUAL COMPRENDE : i) CALENTAR LA CORRIENTE DE ALIMENTACION DE PETROLEO CRUDO DE CERCA DE 100°F A CERCA DE 600°F E INTRODUCIR UNA CORRIENTE LATERAL QUE CONTIENE HIDROGENO A DICHA CORRIENTE DE ALIMENTACION Y MEZCLAR DICHAS CORRIENTES PARA OBTENER UNA DISPERSION UNIFORME DE LAS MOLECULAS DE HIDROGENO EN DICHA CORRIENTE DE PETROLEO, DIVIDIENDO DICHA CORRIENTE MEZCLADA E INTRODUCIENDO UNA CORRIENTE MENOR EN UN TANQUE PRIMARIO PARA OBTENER LA SEPARACION DE FRACCIONES LIGERAS VOLATILES PROVENIENTES DE LOS CORTES MAS PESADOS HIDROGENADOS E INTRODUCIR UNA PORCION MAYOR A UN VAPOR RETORNADO DESDE LA ZONA PRIMARIA DE TRATAMIENTO DE HIDROGENO Y ANTES DE INTRODUCIR A DICHO TANQUE PRIMARIO PARA DETENER EL TRATAMIENTO CON HIDROGENO Y MINIMIZAR LA PRODUCCION DE COQUE EN DICHO TANQUE PRIMARIO; ii) REMOVER LOS VOLATILES LIVIANOS DE DICHO TANQUE PRIMARIO Y DIRIGIRLOS A UN TANQUE SECUNDARIO PARA SEPARACION ADICIONAL; Y iii) REMOVER LA FRACCION NO VOLATIL PESADA DE DICHO TANQUE PRIMARIO Y RECIRCULARLO AL TANQUE PRIMARIO, LUEGO MEZCLARLOS Y CALENTARLOS DE CERCA DE 650°F A CERCA DE 950°F SEGUIDO POR UN MEZCLADO ADICIONAL PARA MEJORAR LAS REACCIONES DE HIDROGENO. DICHO PROCESO ES PARA EL TRATAMIENTO DE PETROLEO CRUDO O PETROLEO CRUDO PARCIALMENTE MEJORADO
PE1999000980A 1998-09-29 1999-09-28 Proceso para mejorar el petroleo crudo usando hidrogeno PE20001200A1 (es)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CA002249051A CA2249051A1 (en) 1998-09-29 1998-09-29 Process for upgrading crude oil using low pressure hydrogen

Publications (1)

Publication Number Publication Date
PE20001200A1 true PE20001200A1 (es) 2000-12-15

Family

ID=4162862

Family Applications (1)

Application Number Title Priority Date Filing Date
PE1999000980A PE20001200A1 (es) 1998-09-29 1999-09-28 Proceso para mejorar el petroleo crudo usando hidrogeno

Country Status (7)

Country Link
US (1) US7001502B1 (es)
EP (1) EP1121400A1 (es)
AU (1) AU5846299A (es)
BR (1) BR9914129A (es)
CA (2) CA2249051A1 (es)
PE (1) PE20001200A1 (es)
WO (1) WO2000018854A1 (es)

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US8021539B2 (en) 2007-06-27 2011-09-20 H R D Corporation System and process for hydrodesulfurization, hydrodenitrogenation, or hydrofinishing
US7491856B2 (en) 2007-06-27 2009-02-17 H R D Corporation Method of making alkylene glycols
US7750188B2 (en) * 2007-06-27 2010-07-06 H R D Corporation System and process for the production of aniline and toluenediamine
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CN101942341A (zh) * 2009-07-09 2011-01-12 中国石油化工股份有限公司抚顺石油化工研究院 一种石油蜡类物质加氢改质方法
CN101942326B (zh) * 2009-07-09 2015-01-14 中国石油化工股份有限公司 一种加氢生产低芳溶剂油的方法
CN101942319A (zh) * 2009-07-09 2011-01-12 中国石油化工股份有限公司抚顺石油化工研究院 一种劣质柴油加氢处理方法
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US20110163003A1 (en) * 2010-01-07 2011-07-07 Lourenco Jose J P Upgrading heavy oil by visbreaking
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US10093870B2 (en) 2010-09-07 2018-10-09 Saudi Arabian Oil Company Desulfurization and sulfone removal using a coker
US10093871B2 (en) 2010-09-07 2018-10-09 Saudi Arabian Oil Company Desulfurization and sulfone removal using a coker
US10035960B2 (en) 2010-09-07 2018-07-31 Saudi Arabian Oil Company Process for oxidative desulfurization and sulfone management by gasification
US9574142B2 (en) 2010-09-07 2017-02-21 Saudi Arabian Oil Company Process for oxidative desulfurization and sulfone management by gasification
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CN102465027B (zh) * 2010-11-05 2015-04-15 中国石油化工股份有限公司 一种重馏分油加氢处理方法
CN102465013B (zh) * 2010-11-05 2016-04-13 中国石油化工股份有限公司 一种高芳含柴油加氢改质方法
CN102465011B (zh) * 2010-11-05 2015-07-22 中国石油化工股份有限公司 重馏分油加氢处理方法
CN102465012B (zh) * 2010-11-05 2015-10-21 中国石油化工股份有限公司 一种劣质柴油深度加氢脱硫方法
JP5876575B2 (ja) * 2011-07-29 2016-03-02 サウジ アラビアン オイル カンパニー 流動接触分解プロセス用の水素に富む原料
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Also Published As

Publication number Publication date
AU5846299A (en) 2000-04-17
WO2000018854A1 (en) 2000-04-06
CA2306069C (en) 2007-09-25
EP1121400A1 (en) 2001-08-08
CA2306069A1 (en) 2000-04-06
US7001502B1 (en) 2006-02-21
BR9914129A (pt) 2001-06-19
CA2249051A1 (en) 2000-03-29

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Legal Events

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FG Grant, registration
FD Application declared void or lapsed