CA2943078C - Systeme et procede pour commander et optimiser la valorisation hydrothermique du brut lourd et du bitume - Google Patents

Systeme et procede pour commander et optimiser la valorisation hydrothermique du brut lourd et du bitume Download PDF

Info

Publication number
CA2943078C
CA2943078C CA2943078A CA2943078A CA2943078C CA 2943078 C CA2943078 C CA 2943078C CA 2943078 A CA2943078 A CA 2943078A CA 2943078 A CA2943078 A CA 2943078A CA 2943078 C CA2943078 C CA 2943078C
Authority
CA
Canada
Prior art keywords
process stream
reactor
hco
lhc
max
Prior art date
Legal status (The legal status 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 status listed.)
Active
Application number
CA2943078A
Other languages
English (en)
Other versions
CA2943078A1 (fr
Inventor
W. Marcus Trygstad
W. Marcus Trygstad
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Aduro Energy Inc
Original Assignee
Aduro Energy 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
Priority claimed from US14/218,619 external-priority patent/US9644455B2/en
Application filed by Aduro Energy Inc filed Critical Aduro Energy Inc
Publication of CA2943078A1 publication Critical patent/CA2943078A1/fr
Application granted granted Critical
Publication of CA2943078C publication Critical patent/CA2943078C/fr
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING 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
    • C10G9/00Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
    • C10G9/34Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils by direct contact with inert preheated fluids, e.g. with molten metals or salts
    • C10G9/36Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils by direct contact with inert preheated fluids, e.g. with molten metals or salts with heated gases or vapours
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING 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
    • C10G9/00Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
    • C10G9/14Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils in pipes or coils with or without auxiliary means, e.g. digesters, soaking drums, expansion means
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING 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
    • C10G31/00Refining of hydrocarbon oils, in the absence of hydrogen, by methods not otherwise provided for
    • C10G31/08Refining of hydrocarbon oils, in the absence of hydrogen, by methods not otherwise provided for by treating with water
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING 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
    • C10G47/00Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions
    • C10G47/36Controlling or regulating

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)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Abstract

L'invention concerne un système et un procédé de valorisation d'un liquide à traiter s'écoulant en continu comprenant du pétrole brut lourd (HCO). Un réacteur reçoit le liquide à traiter combiné à de l'eau, à une température d'entrée qui se situe dans une plage d'environ 60 °C à environ 200 °C; le réacteur comprend un ou plusieurs tubes pour le liquide à traiter présentant une longueur combinée d'environ 30 fois la dimension de leurs sections transversales combinées, et chauffe progressivement le liquide à traiter à une température de sortie T(max)1 comprise dans une plage qui s'étend entre environ 260 °C et environ 400 °C; le réacteur maintient le liquide à traiter à une pression suffisante pour assurer qu'il reste en phase unique à T(max)1. Un dispositif de commande ajuste sélectivement le débit du liquide à traiter dans le réacteur afin de maintenir un temps de séjour total supérieur à environ 1 minute et inférieur à environ 25 minutes.
CA2943078A 2014-03-18 2015-03-18 Systeme et procede pour commander et optimiser la valorisation hydrothermique du brut lourd et du bitume Active CA2943078C (fr)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
US14/218,619 US9644455B2 (en) 2013-02-28 2014-03-18 System and method for controlling and optimizing the hydrothermal upgrading of heavy crude oil and bitumen
US14/218,619 2014-03-18
PCT/US2015/021258 WO2015143039A2 (fr) 2014-03-18 2015-03-18 Système et procédé pour commander et optimiser la valorisation hydrothermique du brut lourd et du bitume

Publications (2)

Publication Number Publication Date
CA2943078A1 CA2943078A1 (fr) 2015-09-24
CA2943078C true CA2943078C (fr) 2023-09-19

Family

ID=54145472

Family Applications (1)

Application Number Title Priority Date Filing Date
CA2943078A Active CA2943078C (fr) 2014-03-18 2015-03-18 Systeme et procede pour commander et optimiser la valorisation hydrothermique du brut lourd et du bitume

Country Status (4)

Country Link
EP (1) EP3119858B1 (fr)
CA (1) CA2943078C (fr)
RU (1) RU2687072C2 (fr)
WO (1) WO2015143039A2 (fr)

Family Cites Families (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3607130A (en) * 1969-09-24 1971-09-21 Exxon Research Engineering Co Reformer furnace
US4778586A (en) * 1985-08-30 1988-10-18 Resource Technology Associates Viscosity reduction processing at elevated pressure
US4840725A (en) * 1987-06-19 1989-06-20 The Standard Oil Company Conversion of high boiling liquid organic materials to lower boiling materials
US6048448A (en) * 1997-07-01 2000-04-11 The Coastal Corporation Delayed coking process and method of formulating delayed coking feed charge
US7128827B2 (en) * 2004-01-14 2006-10-31 Kellogg Brown & Root Llc Integrated catalytic cracking and steam pyrolysis process for olefins
RU2277116C1 (ru) * 2005-01-31 2006-05-27 Общество с ограниченной ответственностью "ЛУКОЙЛ-ПЕРМЬ" Способ обессоливания нефти
US7748458B2 (en) * 2006-02-27 2010-07-06 Geosierra Llc Initiation and propagation control of vertical hydraulic fractures in unconsolidated and weakly cemented sediments
US20080099378A1 (en) * 2006-10-31 2008-05-01 Chevron U.S.A. Inc. Process and reactor for upgrading heavy hydrocarbon oils
US20080274017A1 (en) * 2007-05-04 2008-11-06 Boykin Jack W System for the production of synthetic fuels
JP2011088964A (ja) * 2009-10-20 2011-05-06 Jgc Corp 重質油の改質装置及び重質油の改質方法
US20130105362A1 (en) * 2011-11-02 2013-05-02 Marathon Oil Canada Corporation Systems and methods for integrating bitumen extraction with bitumen upg...
US9783742B2 (en) * 2013-02-28 2017-10-10 Aduro Energy, Inc. System and method for controlling and optimizing the hydrothermal upgrading of heavy crude oil and bitumen

Also Published As

Publication number Publication date
EP3119858A4 (fr) 2017-11-22
EP3119858A2 (fr) 2017-01-25
WO2015143039A3 (fr) 2016-01-14
RU2016140701A3 (fr) 2018-10-09
RU2016140701A (ru) 2018-04-20
EP3119858B1 (fr) 2021-04-21
CA2943078A1 (fr) 2015-09-24
WO2015143039A2 (fr) 2015-09-24
RU2687072C2 (ru) 2019-05-07

Similar Documents

Publication Publication Date Title
US10323492B2 (en) System and method for controlling and optimizing the hydrothermal upgrading of heavy crude oil and bitumen
US20090159498A1 (en) Intergrated process for in-field upgrading of hydrocarbons
CN103649273B (zh) 延迟焦化全馏分原油的方法
US20080099377A1 (en) Process for upgrading heavy hydrocarbon oils
US10907455B2 (en) System and process for recovering hydrocarbons using a supercritical fluid
EP2231824A2 (fr) Processus de valorisation de pétrole brut entier par eau chaude sous pression et fluide de récupération
CN107001940A (zh) 双壁反应器中的重油改质方法
US10450518B2 (en) Supercritical water separation process
Shi et al. In-situ upgrading of heavy crude oils inspired by ex-situ petroleum refining processes
BR112016016601B1 (pt) Processo de fluxo contínuo para converter uma matéria-prima orgânica com ponto de fluidez alto em um produto melhorado
CA2902664C (fr) Systeme et procede pour la commande et l'optimisation de la valorisation hydrothermique de petrole brut lourd et de bitume
CN102597180B (zh) 汽油精馏、骤冷水系统和产物回收区中的沉积物减少法
CA2943078C (fr) Systeme et procede pour commander et optimiser la valorisation hydrothermique du brut lourd et du bitume
US10900327B2 (en) System and method for hydrothermal upgrading of fatty acid feedstock
Chen et al. Optimization of Residual Oil Hydrocrackers: Integration of Pump-Free Ebullated Bed Process with Membrane-Aided Gas Recovery System
Wolodko et al. Application of non-metallic materials in oil sands operations
US20110163003A1 (en) Upgrading heavy oil by visbreaking
US11242735B2 (en) System and process for recovering hydrocarbons using a supercritical fluid
CA3113296C (fr) Systeme et procede de recuperation d'hydrocarbures au moyen d'un liquide supercritique
Luhning Removing constraints on oil sands potential: Pipeline transportation of emerging partially upgraded bitumen
Wolodko et al. Opportunities for Polymer Materials in Oil Sands Applications
Du Plessis et al. Petrochemicals from oil sands
Soiket Life Cycle Assessment (LCA) of Oil Sands-Derived Transportation Fuels Produced from the Vapor Solvent-Based Extraction Process
Schleiffer et al. Optimize field upgrading of oil sands with slurry-phase combi-cracking technology

Legal Events

Date Code Title Description
EEER Examination request

Effective date: 20200220

MPN Maintenance fee for patent paid

Free format text: FEE DESCRIPTION TEXT: MF (PATENT, 10TH ANNIV.) - STANDARD

Year of fee payment: 10

U00 Fee paid

Free format text: ST27 STATUS EVENT CODE: A-4-4-U10-U00-U101 (AS PROVIDED BY THE NATIONAL OFFICE); EVENT TEXT: MAINTENANCE REQUEST RECEIVED

Effective date: 20250204

U11 Full renewal or maintenance fee paid

Free format text: ST27 STATUS EVENT CODE: A-4-4-U10-U11-U102 (AS PROVIDED BY THE NATIONAL OFFICE); EVENT TEXT: MAINTENANCE FEE PAYMENT DETERMINED COMPLIANT

Effective date: 20250204

Free format text: ST27 STATUS EVENT CODE: A-4-4-U10-U11-U102 (AS PROVIDED BY THE NATIONAL OFFICE); EVENT TEXT: MAINTENANCE FEE PAYMENT PAID IN FULL

Effective date: 20250204

MPN Maintenance fee for patent paid

Free format text: FEE DESCRIPTION TEXT: MF (PATENT, 11TH ANNIV.) - STANDARD

Year of fee payment: 11

U00 Fee paid

Free format text: ST27 STATUS EVENT CODE: A-4-4-U10-U00-U101 (AS PROVIDED BY THE NATIONAL OFFICE); EVENT TEXT: MAINTENANCE REQUEST RECEIVED

Effective date: 20260217

U11 Full renewal or maintenance fee paid

Free format text: ST27 STATUS EVENT CODE: A-4-4-U10-U11-U102 (AS PROVIDED BY THE NATIONAL OFFICE); EVENT TEXT: MAINTENANCE FEE PAYMENT PAID IN FULL

Effective date: 20260218