BR0009652A - Método para beneficiar uma carga de alimentação de hidrocarboneto pesado, óleo pesado beneficiado, betume beneficiado, reator de pirólise de fluxo ascendente, e, produto lìquido - Google Patents

Método para beneficiar uma carga de alimentação de hidrocarboneto pesado, óleo pesado beneficiado, betume beneficiado, reator de pirólise de fluxo ascendente, e, produto lìquido

Info

Publication number
BR0009652A
BR0009652A BR0009652-0A BR0009652A BR0009652A BR 0009652 A BR0009652 A BR 0009652A BR 0009652 A BR0009652 A BR 0009652A BR 0009652 A BR0009652 A BR 0009652A
Authority
BR
Brazil
Prior art keywords
feed load
load
heavy hydrocarbon
liquid product
hydrocarbon feed
Prior art date
Application number
BR0009652-0A
Other languages
English (en)
Other versions
BR0009652B1 (pt
Inventor
Barry A Freel
Robert G Graham
Original Assignee
Ensyn Group 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 Ensyn Group Inc filed Critical Ensyn Group Inc
Publication of BR0009652A publication Critical patent/BR0009652A/pt
Publication of BR0009652B1 publication Critical patent/BR0009652B1/pt

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B55/00—Coking mineral oils, bitumen, tar, and the like or mixtures thereof with solid carbonaceous material
    • C10B55/02—Coking mineral oils, bitumen, tar, and the like or mixtures thereof with solid carbonaceous material with solid materials
    • C10B55/04—Coking mineral oils, bitumen, tar, and the like or mixtures thereof with solid carbonaceous material with solid materials with moving solid materials
    • 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
    • C10G31/00—Refining of hydrocarbon oils, in the absence of hydrogen, by methods not otherwise provided for
    • C10G31/06—Refining of hydrocarbon oils, in the absence of hydrogen, by methods not otherwise provided for by heating, cooling, or pressure treatment
    • 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
    • C10G9/00—Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
    • C10G9/28—Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid material
    • C10G9/32—Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid material 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
    • C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/20—Characteristics of the feedstock or the products
    • C10G2300/201—Impurities
    • 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
    • C10G2300/20—Characteristics of the feedstock or the products
    • C10G2300/201—Impurities
    • C10G2300/208—Sediments, e.g. bottom sediment and water or BSW
    • 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
    • C10G2300/20—Characteristics of the feedstock or the products
    • C10G2300/30—Physical properties of feedstocks or products
    • C10G2300/302—Viscosity
    • 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
    • C10G2300/20—Characteristics of the feedstock or the products
    • C10G2300/30—Physical properties of feedstocks or products
    • C10G2300/304—Pour point, cloud point, cold flow properties
    • 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
    • C10G2300/20—Characteristics of the feedstock or the products
    • C10G2300/30—Physical properties of feedstocks or products
    • C10G2300/308—Gravity, density, e.g. API

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)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Materials Engineering (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Abstract

"MéTODO PARA BENEFICIAR UMA CARGA DE ALIMENTAçãO DE HIDROCARBONETO PESADO, óLEO PESADO BENEFICIADO, BETUME BENEFICIADO, REATOR DE PIRóLISE DE FLUXO ASCENDENTE, E, PRODUTO LìQUIDO". A presente invenção é dirigida ao beneficiamento de cargas de alimentação de hidrocarboneto pesado que usa um reator pirolítico de tempo de residência curto operando sob condições que craqueiam e quimicamente beneficiam a carga de alimentação. O processo d presente invenção provê a preparação de uma carga de alimentação parcialmente beneficiada demonstrando reduzida viscosidade e aumentada densidade API. Este processo remove seletivamente metais, sais, água e nitrogênio da carga de alimentação, enquanto ao mesmo tempo maximiza o rendimento do produto líquido, e minimiza a produção de coque e gás. Além disso, este processo reduz a viscosidade da carga de alimentação a fim de permitir o transporte em oleodutos, se desejado, da carga de alimentação beneficiada com pouca ou nenhuma adição de diluentes. O processo de beneficiamento de uma carga de alimentação de hidrocarboneto pesado compreende a introdução de um veículo térmico particulado em um reator de fluxo ascendente, introduzindo a carga de alimentação de hidrocarboneto pesado no reator de fluxo ascendente em um local acima do veiculo térmico, de modo que uma relação de carga do veiculo térmico particulado para carga de alimentação é de cerca de 15:1 a cerca de 200:1, permitindo à carga de alimentação de hidrocarboneto pesado interagir com o veículo térmico com um tempo de residência menor do que cerca de 1 segundo, para produzir uma corrente de produto, separar a corrente de produto do veículo térmico particulado, regenerar o veículo térmico particulado e coletar um produto gasoso e líquido da corrente de produto.
BRPI0009652-0A 1999-04-07 2000-04-07 processo para produzir e transportar uma carga de alimentação lìquida beneficiada a partir de uma carga de alimentação de hidrocarboneto pesado. BR0009652B1 (pt)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US28795899A 1999-04-07 1999-04-07
PCT/CA2000/000369 WO2000061705A1 (en) 1999-04-07 2000-04-07 Rapid thermal processing of heavy hydrocarbon feedstocks

Publications (2)

Publication Number Publication Date
BR0009652A true BR0009652A (pt) 2002-03-26
BR0009652B1 BR0009652B1 (pt) 2012-04-03

Family

ID=23105118

Family Applications (1)

Application Number Title Priority Date Filing Date
BRPI0009652-0A BR0009652B1 (pt) 1999-04-07 2000-04-07 processo para produzir e transportar uma carga de alimentação lìquida beneficiada a partir de uma carga de alimentação de hidrocarboneto pesado.

Country Status (11)

Country Link
US (1) US20120279825A1 (pt)
EP (2) EP1169412B1 (pt)
AU (1) AU3798300A (pt)
BR (1) BR0009652B1 (pt)
CA (1) CA2369288C (pt)
DK (2) DK1169412T3 (pt)
ES (2) ES2429508T3 (pt)
MX (1) MXPA01010120A (pt)
NO (1) NO20014868L (pt)
PT (2) PT2336274E (pt)
WO (1) WO2000061705A1 (pt)

Families Citing this family (25)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7270743B2 (en) * 2000-09-18 2007-09-18 Ivanhoe Energy, Inc. Products produced form rapid thermal processing of heavy hydrocarbon feedstocks
US8062503B2 (en) 2001-09-18 2011-11-22 Ivanhoe Energy Inc. Products produced from rapid thermal processing of heavy hydrocarbon feedstocks
CA2440452A1 (en) 2001-04-20 2002-10-31 Exxonmobil Upstream Research Company Heavy oil upgrade method and apparatus
US8888992B2 (en) 2005-08-09 2014-11-18 Uop Llc Process and apparatus for improving flow properties of crude petroleum
WO2007112570A1 (en) 2006-04-03 2007-10-11 Pharmatherm Chemicals Inc. Thermal extraction method and product
CA2624746C (en) 2007-03-12 2015-02-24 Robert Graham Methods and systems for producing reduced resid and bottomless products from heavy hydrocarbon feedstocks
US7905990B2 (en) * 2007-11-20 2011-03-15 Ensyn Renewables, Inc. Rapid thermal conversion of biomass
US20110284359A1 (en) 2010-05-20 2011-11-24 Uop Llc Processes for controlling afterburn in a reheater and for controlling loss of entrained solid particles in combustion product flue gas
US8499702B2 (en) 2010-07-15 2013-08-06 Ensyn Renewables, Inc. Char-handling processes in a pyrolysis system
CN102382667B (zh) * 2010-09-01 2013-12-25 中国石油化工股份有限公司 一种煤裂解和重质油裂解的联合生产方法
JP2014507265A (ja) 2010-12-29 2014-03-27 アイヴァンホー エナジー インコーポレイテッド リフトガスを分配する方法、システム、および装置
US9441887B2 (en) 2011-02-22 2016-09-13 Ensyn Renewables, Inc. Heat removal and recovery in biomass pyrolysis
US9347005B2 (en) 2011-09-13 2016-05-24 Ensyn Renewables, Inc. Methods and apparatuses for rapid thermal processing of carbonaceous material
US10400175B2 (en) 2011-09-22 2019-09-03 Ensyn Renewables, Inc. Apparatuses and methods for controlling heat for rapid thermal processing of carbonaceous material
US10041667B2 (en) 2011-09-22 2018-08-07 Ensyn Renewables, Inc. Apparatuses for controlling heat for rapid thermal processing of carbonaceous material and methods for the same
US9044727B2 (en) 2011-09-22 2015-06-02 Ensyn Renewables, Inc. Apparatuses and methods for controlling heat for rapid thermal processing of carbonaceous material
US9109177B2 (en) 2011-12-12 2015-08-18 Ensyn Renewables, Inc. Systems and methods for renewable fuel
US9670413B2 (en) 2012-06-28 2017-06-06 Ensyn Renewables, Inc. Methods and apparatuses for thermally converting biomass
US9707532B1 (en) 2013-03-04 2017-07-18 Ivanhoe Htl Petroleum Ltd. HTL reactor geometry
AR097135A1 (es) 2013-06-26 2016-02-24 Ensyn Renewables Inc Sistemas y métodos para combustible renovable
WO2016123489A1 (en) * 2015-01-30 2016-08-04 Fbp Corp Fast pyrolysis method for upgrading heavy crude oil
DK3337966T3 (da) 2015-08-21 2022-02-28 Ensyn Renewables Inc Opvarmningssystem med flydende biomasse
CA3048681A1 (en) 2016-12-29 2018-07-05 Ensyn Renewables, Inc. Demetallization of liquid biomass
CA2963436C (en) 2017-04-06 2022-09-20 Iftikhar Huq Partial upgrading of bitumen
CN114989846A (zh) * 2022-06-16 2022-09-02 上海电气集团股份有限公司 一种塑料热裂解系统和方法

Family Cites Families (33)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3375175A (en) * 1965-01-21 1968-03-26 Fmc Corp Pyrolysis of coal
US4166786A (en) * 1976-06-25 1979-09-04 Occidental Petroleum Corporation Pyrolysis and hydrogenation process
US4080285A (en) * 1976-07-12 1978-03-21 Gulf Research & Development Company Thermal cracking of shale oil
US4153540A (en) * 1977-05-04 1979-05-08 Mobil Oil Corporation Upgrading shale oil
CA1097245A (en) 1977-11-22 1981-03-10 Chandra P. Khulbe Thermal hydrocracking of heavy hydrocarbon oils with heavy oil recycle
US4161442A (en) 1978-01-05 1979-07-17 Mobil Oil Corporation Processing of tar sands
US4243514A (en) 1979-05-14 1981-01-06 Engelhard Minerals & Chemicals Corporation Preparation of FCC charge from residual fractions
US4263128A (en) 1978-02-06 1981-04-21 Engelhard Minerals & Chemicals Corporation Upgrading petroleum and residual fractions thereof
US4232514A (en) 1979-06-20 1980-11-11 General Motors Corporation Dump control for turbine engine gate valve actuator
US4311580A (en) 1979-11-01 1982-01-19 Engelhard Minerals & Chemicals Corporation Selective vaporization process and dynamic control thereof
US4328091A (en) 1979-11-01 1982-05-04 Engelhard Minerals & Chemicals Corporation Selective vaporization process
US4294686A (en) 1980-03-11 1981-10-13 Gulf Canada Limited Process for upgrading heavy hydrocarbonaceous oils
US4446009A (en) 1980-06-02 1984-05-01 Engelhard Corporation Selective vaporization process and apparatus
US4569753A (en) 1981-09-01 1986-02-11 Ashland Oil, Inc. Oil upgrading by thermal and catalytic cracking
US4490234A (en) 1982-02-22 1984-12-25 Beckman Instruments, Inc. Method for measuring ionic concentration utilizing an ion-sensing electrode
GB2117394B (en) * 1982-03-22 1986-05-21 Engelhard Corp Decarbonizing and demetallizing petroleum stocks
US4435272A (en) 1982-04-16 1984-03-06 Engelhard Corporation Process for upgrading crude oil and residual fractions thereof by vaporizing the charge in a falling curtain of contact particles
US4427539A (en) 1982-09-07 1984-01-24 Ashland Oil, Inc. Demetallizing and decarbonizing heavy residual oil feeds
DE3310712C2 (de) * 1983-03-24 1994-02-24 Metallgesellschaft Ag, 6000 Frankfurt Verfahren zum Behandeln eines wasserhaltigen Kondensats
JPS60248793A (ja) 1984-05-22 1985-12-09 Fuji Standard Res Kk 重質油の熱分解法
US4818373A (en) 1984-10-19 1989-04-04 Engelhard Corporation Process for upgrading tar and bitumen
US4578183A (en) 1984-11-30 1986-03-25 Mobil Oil Corporation Feed mixing technique for fluidized catalytic cracking of hydrocarbon oil
JPH0662958B2 (ja) 1985-02-28 1994-08-17 富士スタンダ−ドリサ−チ株式会社 重質油の熱分解法
US4985136A (en) 1987-11-05 1991-01-15 Bartholic David B Ultra-short contact time fluidized catalytic cracking process
US4980045A (en) 1988-08-02 1990-12-25 Chevron Research Company Heavy oil pretreatment process with reduced sulfur oxide emissions
US5792340A (en) 1990-01-31 1998-08-11 Ensyn Technologies, Inc. Method and apparatus for a circulating bed transport fast pyrolysis reactor system
CA2009021C (en) 1990-01-31 2001-09-11 Barry A. Freel Method and apparatus for a circulating bed transport fast pyrolysis reactor system
CA2012071C (en) * 1990-03-13 1994-03-08 Theo J. W. Bruijn Upgrading oil emulsions with carbon monoxide or synthesis gas
US5413702A (en) 1992-02-21 1995-05-09 Mobil Oil Corporation High severity visbreaking of residual oil
US5296131A (en) 1992-12-02 1994-03-22 Mobil Oil Corporation Process for short contact time cracking
US5662868A (en) 1994-09-22 1997-09-02 Stone & Webster Engineering Corporation Short residence time cracking apparatus and process
US5723040A (en) 1994-09-22 1998-03-03 Stone & Webster Engineering Corporation Fluid catalytic cracking process and apparatus
US5807478A (en) * 1997-05-16 1998-09-15 Exxon Research And Engineering Company Bitumen modification using fly ash derived from bitumen coke

Also Published As

Publication number Publication date
DK2336274T3 (da) 2013-09-30
WO2000061705A1 (en) 2000-10-19
NO20014868L (no) 2001-12-06
PT1169412E (pt) 2013-09-23
CA2369288C (en) 2011-05-24
ES2429816T3 (es) 2013-11-18
US20120279825A1 (en) 2012-11-08
DK1169412T3 (da) 2013-09-30
PT2336274E (pt) 2013-09-25
MXPA01010120A (es) 2002-08-12
AU3798300A (en) 2000-11-14
NO20014868D0 (no) 2001-10-05
EP2336274B1 (en) 2013-06-19
EP2336274A1 (en) 2011-06-22
EP1169412B1 (en) 2013-06-19
EP1169412A1 (en) 2002-01-09
ES2429508T3 (es) 2013-11-15
BR0009652B1 (pt) 2012-04-03
CA2369288A1 (en) 2000-10-19

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