AR086012A1 - Procedimiento para licuar una fraccion de partida rica en hidrocarburos - Google Patents

Procedimiento para licuar una fraccion de partida rica en hidrocarburos

Info

Publication number
AR086012A1
AR086012A1 ARP120101294A ARP120101294A AR086012A1 AR 086012 A1 AR086012 A1 AR 086012A1 AR P120101294 A ARP120101294 A AR P120101294A AR P120101294 A ARP120101294 A AR P120101294A AR 086012 A1 AR086012 A1 AR 086012A1
Authority
AR
Argentina
Prior art keywords
fraction
nitrogen
stream
starting fraction
exchange process
Prior art date
Application number
ARP120101294A
Other languages
English (en)
Inventor
Sandes Emanuel Freire
Silva Leandro Morais
William Richard Gilbert
Ramos Jose Geraldo Furtado
Original Assignee
Petroleo Brasileiro Sa
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 Petroleo Brasileiro Sa filed Critical Petroleo Brasileiro Sa
Publication of AR086012A1 publication Critical patent/AR086012A1/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
    • C10G11/00—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
    • C10G11/14—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts
    • C10G11/18—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts according to the "fluidised-bed" technique
    • 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
    • C10G51/06—Treatment of hydrocarbon oils, in the absence of hydrogen, by two or more cracking processes only plural parallel stages 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
    • C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/10—Feedstock materials
    • C10G2300/1037—Hydrocarbon fractions
    • C10G2300/1048—Middle distillates
    • 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
    • C10G2300/4056—Retrofitting operations
    • 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
    • C10G2400/02—Gasoline
    • 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
    • C10G2400/04—Diesel oil

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)
  • Separation By Low-Temperature Treatments (AREA)

Abstract

Se describe un procedimiento para licuar una fracción de partida rica en hidrocarburos, preferiblemente de gas contra un circuito de refrigeración por nitrógeno, teniendo lugar el enfriamiento de la fracción de partida contra una corriente de nitrógeno gaseoso a calentar y la licuación de la fracción de partida contra una corriente de nitrógeno líquido, a evaporar. Inventivamente: el enfriamiento y la licuación de la fracción de partida tiene lugar en un proceso de intercambio de calor de al menos tres etapas (E1a - E1c), siendo en una primera sección del proceso de intercambio de calor (E1a) enfriada la fracción de partida (1) contra una comente de nitrógeno gaseosa a sobrecalentar (9) en una medida tal que se puede llevar a cabo una separación sustancialmente completa (D2) de los componentes pesados (2’), siendo en una segunda sección del proceso de intercambio de calor (E1b) licuada parcialmente la fracción de partida (2), liberada de los componentes pesados, contra una corriente de nitrógeno gaseoso a sobrecalentar (9), y siendo licuada en la tercera sección del proceso de intercambio de calor (E1c) la fracción de partida (2) contra una corriente de nitrógeno a evaporar parcialmente (8).
ARP120101294A 2011-04-15 2012-04-13 Procedimiento para licuar una fraccion de partida rica en hidrocarburos AR086012A1 (es)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
PCT/BR2011/000108 WO2012139181A1 (pt) 2011-04-15 2011-04-15 Processo de fcc para a maximização de diesel utilizando dois conversores distintos

Publications (1)

Publication Number Publication Date
AR086012A1 true AR086012A1 (es) 2013-11-13

Family

ID=47008720

Family Applications (1)

Application Number Title Priority Date Filing Date
ARP120101294A AR086012A1 (es) 2011-04-15 2012-04-13 Procedimiento para licuar una fraccion de partida rica en hidrocarburos

Country Status (5)

Country Link
US (1) US20140034551A1 (es)
JP (1) JP6068437B2 (es)
AR (1) AR086012A1 (es)
BR (1) BR112013019604B1 (es)
WO (1) WO2012139181A1 (es)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20150136647A1 (en) * 2013-11-21 2015-05-21 Kellogg Brown & Root Llc Reactor and main fractionator configuration for producing diesel
TW202104562A (zh) * 2019-04-03 2021-02-01 美商魯瑪斯科技有限責任公司 用於升級輕油系列材料之合併有固體分離裝置之分段流體化媒裂程序
US20220081624A1 (en) * 2020-09-14 2022-03-17 Saudi Arabian Oil Company Methods for upgrading hydrocarbon feeds to produce olefins
CN112420132A (zh) * 2020-10-29 2021-02-26 重庆大学 一种汽油催化裂化过程产品质量优化控制方法

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US5009769A (en) * 1989-02-06 1991-04-23 Stone & Webster Engineering Corporation Process for catalytic cracking of hydrocarbons
JP4361234B2 (ja) * 1999-06-23 2009-11-11 中國石油化工集團公司 ディーゼル油の収率と液化ガスの収率を同時に増加させる接触分解法
ATE370917T1 (de) * 2002-06-25 2007-09-15 Albemarle Netherlands Bv Verwendung von kationischen schichtmaterialien, zusammensetzungen dieser materialien und die herstellung von kationischen schichtmaterialien
BR0312235A (pt) * 2002-06-28 2005-04-12 Albemarle Netherlands Bv Catalisador de fcc para redução do conteúdo de enxofre em gasolina e diesel
US7074321B1 (en) * 2002-11-12 2006-07-11 Uop Llc Combination hydrocracking process for the production of low sulfur motor fuels
US20060231459A1 (en) * 2005-03-28 2006-10-19 Swan George A Iii FCC process combining molecular separation with staged conversion
US7601254B2 (en) * 2005-05-19 2009-10-13 Uop Llc Integrated fluid catalytic cracking process
FR2886941B1 (fr) * 2005-06-09 2010-02-12 Inst Francais Du Petrole Procede d'hydrocraquage doux incluant une dilution de la charge
BRPI0502577B1 (pt) * 2005-07-07 2015-11-03 Petroleo Brasileiro Sa processo de craqueamento catalítico para produção de diesel a partir de óleos vegetais
BRPI0504321B1 (pt) * 2005-10-07 2015-04-22 Petroleo Brasileiro Sa Processo e aparato para a maximização de destilados médios de fcc
EA016228B1 (ru) * 2005-12-22 2012-03-30 Альбемарл Недерландс Бв Способ каталитического крекинга со взвешенным катализатором
WO2008020551A1 (en) * 2006-08-18 2008-02-21 Nippon Oil Corporation Method of treating biomass, fuel for fuel cell, gasoline, diesel fuel, liquefied petroleum gas, and synthetic resin
WO2008148686A1 (en) * 2007-06-08 2008-12-11 Albemarle Netherlands, B.V. Catalytic cracking and hydroprocessing process for high diesel yield with low aromatic content and/or high propylene yield
BRPI0702541A2 (pt) * 2007-06-21 2009-02-10 Petroleo Brasileiro Sa processo de craqueamento catalÍtico para produÇço de diesel a partir de sementes de oleaginosas
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BRPI0704422A2 (pt) * 2007-10-29 2009-06-23 Petroleo Brasileiro Sa sistema catalìtico e aditivo para maximização de olefinas leves em unidades de craqueamento catalìtico fluido em operações de baixa severidade
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Also Published As

Publication number Publication date
BR112013019604A2 (pt) 2016-10-04
US20140034551A1 (en) 2014-02-06
JP2014510817A (ja) 2014-05-01
BR112013019604B1 (pt) 2018-10-16
JP6068437B2 (ja) 2017-01-25
WO2012139181A1 (pt) 2012-10-18
WO2012139181A8 (pt) 2012-12-13

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