BRPI0410096A - método para combinar um resìduo de hidrocarboneto pesado de um processo de hidroconversão de resìduo, e, combinação transportável por tubulação - Google Patents

método para combinar um resìduo de hidrocarboneto pesado de um processo de hidroconversão de resìduo, e, combinação transportável por tubulação

Info

Publication number
BRPI0410096A
BRPI0410096A BRPI0410096-4A BRPI0410096A BRPI0410096A BR PI0410096 A BRPI0410096 A BR PI0410096A BR PI0410096 A BRPI0410096 A BR PI0410096A BR PI0410096 A BRPI0410096 A BR PI0410096A
Authority
BR
Brazil
Prior art keywords
combination
combining
hydroconversion process
waste
heavy
Prior art date
Application number
BRPI0410096-4A
Other languages
English (en)
Inventor
Franciscus Gondulfus Anto Berg
Scott John Fryer
Mashall Glenn Letts
Michael Robert Margerum
William James Power
Oscar Kui Yin Sy
Larry Vadori
Original Assignee
Shell Int Research
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 Shell Int Research filed Critical Shell Int Research
Publication of BRPI0410096A publication Critical patent/BRPI0410096A/pt
Publication of BRPI0410096B1 publication Critical patent/BRPI0410096B1/pt

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
    • 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
    • C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/10—Feedstock materials
    • C10G2300/1033—Oil well production fluids
    • 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
    • C10G2300/107—Atmospheric residues having a boiling point of at least about 538 °C
    • 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
    • C10G2300/1077—Vacuum residues
    • 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
    • C10G2300/205—Metal content
    • C10G2300/206—Asphaltenes
    • 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
    • C10G2300/301—Boiling range
    • 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
    • C10G2300/80—Additives
    • C10G2300/802—Diluents

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

"MéTODO PARA COMBINAR UM RESìDUO DE HIDROCARBONETO PESADO DE UM PROCESSO DE HIDROCONVERSãO DE RESìDUO, E, COMBINAçãO TRANSPORTáVEL POR TUBULAçãO". é divulgado um método para produzir uma combinação estável transportável por tubulação a partir de um resíduo pesado de um processo de hidroconversão catalitica operando com altas razões de conversão (60-80 %), pela combinação do resíduo pesado com um betume virgem, tal como um betume produzido dos depósitos de óleo em areia de Peace River ou Cold Lake, em Alberta, Canadá, e/ou com um óleo cru virgem de Wabasca, onde a Fração 524<198>C+ da combinação é controlada de tal modo que: 1) A combinação compreende menos de 40% em volume dos componentes 524<198>C+ pesados, isto é componentes que ebulem, na pressão atmosférica, a uma temperatura acima de 524 Graus Celsius; e 2) A fração 524<198>C+ na combinação compreende menos de cerca de 80% em volume de resíduo pesado originado do processo de hidroconversão.
BRPI0410096-4B1A 2003-05-09 2004-05-07 mÉtodo para combinar um resÍduo de hidrocarboneto pesado de um processo de hidroconversço de resÍduo, e, combinaÇço transportÁvel por tubulaÇço BRPI0410096B1 (pt)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
CA2428369A CA2428369C (en) 2003-05-09 2003-05-09 Method of producing a pipelineable blend from a heavy residue of a hydroconversion process
PCT/EP2004/050733 WO2004099349A1 (en) 2003-05-09 2004-05-07 Method of producing a pipelineable blend from a heavy residue of a hydroconversion process

Publications (2)

Publication Number Publication Date
BRPI0410096A true BRPI0410096A (pt) 2006-05-16
BRPI0410096B1 BRPI0410096B1 (pt) 2013-09-24

Family

ID=33426218

Family Applications (1)

Application Number Title Priority Date Filing Date
BRPI0410096-4B1A BRPI0410096B1 (pt) 2003-05-09 2004-05-07 mÉtodo para combinar um resÍduo de hidrocarboneto pesado de um processo de hidroconversço de resÍduo, e, combinaÇço transportÁvel por tubulaÇço

Country Status (8)

Country Link
US (1) US7799206B2 (pt)
EP (1) EP1620530A1 (pt)
CN (1) CN100473713C (pt)
AU (1) AU2004236441B2 (pt)
BR (1) BRPI0410096B1 (pt)
CA (1) CA2428369C (pt)
EA (1) EA008392B1 (pt)
WO (1) WO2004099349A1 (pt)

Families Citing this family (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8002968B2 (en) 2005-11-14 2011-08-23 Statoil Canada Ltd. Process for treating a heavy hydrocarbon feedstock and a product obtained therefrom
US7837855B2 (en) * 2006-08-21 2010-11-23 Exxonmobil Research & Engineering Company High-solvency-dispersive-power (HSDP) crude oil blending for fouling mitigation and on-line cleaning
US7901564B2 (en) * 2006-08-21 2011-03-08 Exxonmobil Research & Engineering Company Mitigation of refinery process unit fouling using high-solvency-dispersive-power (HSDP) resid fractions
US8440069B2 (en) * 2007-08-06 2013-05-14 Exxonmobil Research And Engineering Company Methods of isolating and using components from a high solvency dispersive power (HSDP) crude oil
US8062504B2 (en) * 2007-08-06 2011-11-22 Exxonmobil Research & Engineering Company Method for reducing oil fouling in heat transfer equipment
US8425761B2 (en) * 2008-12-11 2013-04-23 Exxonmobil Research And Engineering Company Non-high solvency dispersive power (non-HSDP) crude oil with increased fouling mitigation and on-line cleaning effects
US8916041B2 (en) * 2011-12-23 2014-12-23 Shell Oil Company Blending hydrocarbon streams to prevent fouling
US20130184382A1 (en) * 2012-01-12 2013-07-18 Baker Hughes Incorporated Process for preparing blends of bitumen having known stability properties
KR101287300B1 (ko) 2012-04-17 2013-07-17 에스케이에너지 주식회사 안정화된 탄화수소 오일 블렌드의 제조방법
US9773097B2 (en) * 2014-08-06 2017-09-26 Yokogawa Electric Corporation System and method of optimizing blending ratios for producing product
CN104565824B (zh) * 2014-12-22 2016-03-02 山东东明石化集团有限公司 一种长距离管道常温掺输玛瑞原油的方法
EP3473569A1 (en) * 2016-01-06 2019-04-24 Oren Technologies, LLC Conveyor with integrated dust collector system
RU2743698C1 (ru) * 2020-06-23 2021-02-24 Публичное акционерное общество "Славнефть-Ярославнефтеоргсинтез", (ПАО "Славнефть-ЯНОС") Способ переработки непревращенных остатков переработки нефти

Family Cites Families (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4411768A (en) * 1979-12-21 1983-10-25 The Lummus Company Hydrogenation of high boiling hydrocarbons
US4728412A (en) * 1986-09-19 1988-03-01 Amoco Corporation Pour-point depression of crude oils by addition of tar sand bitumen
US5320741A (en) * 1992-04-09 1994-06-14 Stone & Webster Engineering Corporation Combination process for the pretreatment and hydroconversion of heavy residual oils
US5871634A (en) * 1996-12-10 1999-02-16 Exxon Research And Engineering Company Process for blending potentially incompatible petroleum oils
US5807478A (en) * 1997-05-16 1998-09-15 Exxon Research And Engineering Company Bitumen modification using fly ash derived from bitumen coke
US6096192A (en) 1998-07-14 2000-08-01 Exxon Research And Engineering Co. Producing pipelinable bitumen
US6355159B1 (en) 2000-08-04 2002-03-12 Exxonmobil Research And Engineering Company Dissolution and stabilization of thermally converted bitumen

Also Published As

Publication number Publication date
CN1784482A (zh) 2006-06-07
EA200501769A1 (ru) 2006-04-28
CN100473713C (zh) 2009-04-01
US20070023323A1 (en) 2007-02-01
EP1620530A1 (en) 2006-02-01
US7799206B2 (en) 2010-09-21
CA2428369C (en) 2012-10-30
EA008392B1 (ru) 2007-04-27
AU2004236441A1 (en) 2004-11-18
CA2428369A1 (en) 2004-11-09
WO2004099349A1 (en) 2004-11-18
BRPI0410096B1 (pt) 2013-09-24
AU2004236441B2 (en) 2007-08-16

Similar Documents

Publication Publication Date Title
BRPI0410096A (pt) método para combinar um resìduo de hidrocarboneto pesado de um processo de hidroconversão de resìduo, e, combinação transportável por tubulação
Li et al. A review of in situ upgrading technology for heavy crude oil
Yang et al. Investigating pilot test of oil shale pyrolysis and oil and gas upgrading by water vapor injection
Fan et al. Studies on the synergetic effects of mineral and steam on the composition changes of heavy oils
Tayfun Statistics of nonlinear wave crests and groups
Zhao et al. Using hydrogen donor with oil-soluble catalysts for upgrading heavy oil
US20130161008A1 (en) Preparation and use of nano-catalysts for in-situ reaction with kerogen
WO2012088476A2 (en) In-situ kerogen conversion and recovery
Hart The novel THAI–CAPRI technology and its comparison to other thermal methods for heavy oil recovery and upgrading
Lyadov et al. Extraction and refining of heavy crude oils: problems and prospects
BR0114280A (pt) Processo de produção de diesel por hidrocraqueamento de pressão moderada
BRPI0412200A (pt) método de controlar a temperatura de uma reação exotérmica
Xie et al. Reaction kinetics study on hydrocarbon generation of medium-and low-maturity organic-rich shale in supercritical water
US4514283A (en) Process for separating and converting heavy oil asphaltenes in a field location
EA201070405A1 (ru) Способ эффективного использования теплоты от трубчатой установки для риформинга
Pang et al. Study on Hydrothermal Cracking of Heavy Oil under the Coexisting Conditions of Supercritical Water and Non-condensate Gas
Kwofie et al. The effect of reaction time and temperature on the aquathermolysis process of heavy crude oil
Yang et al. Evolution of microstructure of full lamellar titanium alloy BT18Y solutionized at α+ β phase field
Zaykina et al. Prospects for irradiation processing in the petroleum industry
Fu et al. Effects of operating conditions on supercritical methanol liquefaction of polypropylene
Li et al. Review of chemical viscosity reduction technology for ordinary heavy oil reservoirs based on environmental protection
BRPI0510813A (pt) processo para a conversão de um condensado de hidrocarboneto em combustìveis
Zhang et al. Unveiling the changes in the molecular groups of tight sandstones in response to an electric Field
Köseoglu et al. Hydrocracking of Athabasca bitumen: Kinetics of formation of gases
Hong et al. Effective cracking of heavy crude oil by using shock-induced nanobubble collapse: a molecular dynamics study

Legal Events

Date Code Title Description
B09A Decision: intention to grant [chapter 9.1 patent gazette]
B16A Patent or certificate of addition of invention granted [chapter 16.1 patent gazette]

Free format text: PRAZO DE VALIDADE: 20 (VINTE) ANOS CONTADOS A PARTIR DE 07/05/2004, OBSERVADAS AS CONDICOES LEGAIS.

B21F Lapse acc. art. 78, item iv - on non-payment of the annual fees in time

Free format text: REFERENTE A 19A ANUIDADE.

B24J Lapse because of non-payment of annual fees (definitively: art 78 iv lpi, resolution 113/2013 art. 12)

Free format text: EM VIRTUDE DA EXTINCAO PUBLICADA NA RPI 2721 DE 28-02-2023 E CONSIDERANDO AUSENCIA DE MANIFESTACAO DENTRO DOS PRAZOS LEGAIS, INFORMO QUE CABE SER MANTIDA A EXTINCAO DA PATENTE E SEUS CERTIFICADOS, CONFORME O DISPOSTO NO ARTIGO 12, DA RESOLUCAO 113/2013.