AR086012A1 - PROCEDURE FOR LIQUIDING A FRACTION OF HYDROCARBON RICH START - Google Patents

PROCEDURE FOR LIQUIDING A FRACTION OF HYDROCARBON RICH START

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
Spanish (es)
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/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
    • 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

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).A process for liquefying a hydrocarbon-rich starting fraction, preferably gas against a nitrogen cooling circuit, is described, cooling of the starting fraction against a stream of gaseous nitrogen to be heated and liquefaction of the starting fraction against a stream of liquid nitrogen, to evaporate. Inventively: the cooling and liquefaction of the starting fraction takes place in a heat exchange process of at least three stages (E1a-E1c), the fraction of heat being cooled in a first section of the heat exchange process (E1a) heading (1) against a gaseous nitrogen source to be superheated (9) in such a way that a substantially complete separation (D2) of the heavy components (2 ') can be carried out, being in a second section of the exchange process of heat (E1b) partially liquefied the starting fraction (2), released from the heavy components, against a stream of nitrogen gas to be superheated (9), and being liquefied in the third section of the heat exchange process (E1c) the Starting fraction (2) against a stream of nitrogen to be partially evaporated (8).

ARP120101294A 2011-04-15 2012-04-13 PROCEDURE FOR LIQUIDING A FRACTION OF HYDROCARBON RICH START AR086012A1 (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
PCT/BR2011/000108 WO2012139181A1 (en) 2011-04-15 2011-04-15 Fcc process for diesel maximization using two distinct converters

Publications (1)

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

Family

ID=47008720

Family Applications (1)

Application Number Title Priority Date Filing Date
ARP120101294A AR086012A1 (en) 2011-04-15 2012-04-13 PROCEDURE FOR LIQUIDING A FRACTION OF HYDROCARBON RICH START

Country Status (5)

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

Families Citing this family (4)

* Cited by examiner, † Cited by third party
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US20150136647A1 (en) * 2013-11-21 2015-05-21 Kellogg Brown & Root Llc Reactor and main fractionator configuration for producing diesel
TW202104562A (en) * 2019-04-03 2021-02-01 美商魯瑪斯科技有限責任公司 Staged fluid catalytic cracking processes incorporating a solids separation device for upgrading naphtha range material
US20220081624A1 (en) * 2020-09-14 2022-03-17 Saudi Arabian Oil Company Methods for upgrading hydrocarbon feeds to produce olefins
CN112420132A (en) * 2020-10-29 2021-02-26 重庆大学 Product quality optimization control method in gasoline catalytic cracking process

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US5009769A (en) * 1989-02-06 1991-04-23 Stone & Webster Engineering Corporation Process for catalytic cracking of hydrocarbons
JP4361234B2 (en) * 1999-06-23 2009-11-11 中國石油化工集團公司 Catalytic cracking method to simultaneously increase the yield of diesel oil and the yield of liquefied gas
DE60315835T2 (en) * 2002-06-25 2008-05-21 Albemarle Netherlands B.V. USE OF CATIONIC LAYER MATERIALS, COMPOSITIONS OF THESE MATERIALS, AND THE PREPARATION OF CATIONIC LAYER MATERIALS
EP1517747A1 (en) * 2002-06-28 2005-03-30 Albemarle Netherlands B.V. Fcc catalyst for reducing the sulfur content in gasoline and 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 (en) * 2005-06-09 2010-02-12 Inst Francais Du Petrole SOFT HYDROCRACKING PROCESS INCLUDING DILUTION OF THE LOAD
BRPI0502577B1 (en) * 2005-07-07 2015-11-03 Petroleo Brasileiro Sa catalytic cracking process for diesel production from vegetable oils
BRPI0504321B1 (en) * 2005-10-07 2015-04-22 Petroleo Brasileiro Sa Process and apparatus for maximizing fcc average distillates
KR20080081048A (en) * 2005-12-22 2008-09-05 알베마를 네덜란드 비.브이. Novel cracking catalytic compositions
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 (en) * 2007-06-21 2009-02-10 Petroleo Brasileiro Sa catalytic cracking process for diesel production from oilseeds
US20090065393A1 (en) * 2007-09-07 2009-03-12 Uop, Llc Fluid catalytic cracking and hydrotreating processes for fabricating diesel fuel from waxes
BRPI0704422A2 (en) * 2007-10-29 2009-06-23 Petroleo Brasileiro Sa catalytic and additive system for maximizing light olefins in fluid catalytic cracking units in low severity operations
BRPI0800236B1 (en) * 2008-01-24 2019-05-14 Petroleo Brasileiro S.A. - Petrobras FLUID CATALYTIC CRACKING PROCESS AND EQUIPMENT FOR THE PRODUCTION OF LOW AROMATIC MEDIUM DISTILLED
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FR2959748B1 (en) * 2010-05-06 2012-05-18 Inst Francais Du Petrole CATALYTIC CRACKING PROCESS WITH RECYCLED OF OLEFIN CUT FROM THE GAS SEPARATION SECTION TO MAXIMIZE PRODUCTION OF PROPYLENE.

Also Published As

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

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