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WO2009086107A3 - Procédé de valorisation du pétrole lourd comprenant la récupération de catalyseur usé - Google Patents

Procédé de valorisation du pétrole lourd comprenant la récupération de catalyseur usé Download PDF

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Publication number
WO2009086107A3
WO2009086107A3 PCT/US2008/087682 US2008087682W WO2009086107A3 WO 2009086107 A3 WO2009086107 A3 WO 2009086107A3 US 2008087682 W US2008087682 W US 2008087682W WO 2009086107 A3 WO2009086107 A3 WO 2009086107A3
Authority
WO
WIPO (PCT)
Prior art keywords
catalyst
heavy oil
slurry
solvent
combined
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.)
Ceased
Application number
PCT/US2008/087682
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English (en)
Other versions
WO2009086107A2 (fr
Inventor
Seyi A. Odueyungbo
Lalit S. Shah
Christopher A. Power
James R. Stoy
Fred D. Brent
Bruce E. Reynolds
Andre R. Da Costa
Paul F. Bryan
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.)
Chevron USA Inc
Original Assignee
Chevron USA 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 US12/004,014 external-priority patent/US8722556B2/en
Priority claimed from US12/004,015 external-priority patent/US8765622B2/en
Application filed by Chevron USA Inc filed Critical Chevron USA Inc
Priority to BRPI0821358-5A priority Critical patent/BRPI0821358A2/pt
Priority to CA2709072A priority patent/CA2709072C/fr
Priority to CN2008801251442A priority patent/CN101918516B/zh
Publication of WO2009086107A2 publication Critical patent/WO2009086107A2/fr
Publication of WO2009086107A3 publication Critical patent/WO2009086107A3/fr
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

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    • 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
    • C10G31/09—Refining of hydrocarbon oils, in the absence of hydrogen, by methods not otherwise provided for by filtration
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D63/00—Apparatus in general for separation processes using semi-permeable membranes
    • B01D63/06—Tubular membrane modules
    • B01D63/069—Tubular membrane modules comprising a bundle of tubular membranes
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D61/00—Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
    • B01D61/14—Ultrafiltration; Microfiltration
    • B01D61/145—Ultrafiltration
    • B01D61/146—Ultrafiltration comprising multiple ultrafiltration steps
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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    • B01D61/00—Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
    • B01D61/14—Ultrafiltration; Microfiltration
    • B01D61/147—Microfiltration
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D61/00—Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
    • B01D61/14—Ultrafiltration; Microfiltration
    • B01D61/147—Microfiltration
    • B01D61/1471—Microfiltration comprising multiple microfiltration steps
    • B—PERFORMING OPERATIONS; TRANSPORTING
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    • 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
    • C10G21/00—Refining of hydrocarbon oils, in the absence of hydrogen, by extraction with selective solvents
    • C10G21/06—Refining of hydrocarbon oils, in the absence of hydrogen, by extraction with selective solvents characterised by the solvent used
    • 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
    • C10G49/00—Treatment of hydrocarbon oils, in the presence of hydrogen or hydrogen-generating compounds, not provided for in a single one of groups C10G45/02, C10G45/32, C10G45/44, C10G45/58 or C10G47/00
    • C10G49/02—Treatment of hydrocarbon oils, in the presence of hydrogen or hydrogen-generating compounds, not provided for in a single one of groups C10G45/02, C10G45/32, C10G45/44, C10G45/58 or C10G47/00 characterised by the catalyst used
    • 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
    • C10G49/00—Treatment of hydrocarbon oils, in the presence of hydrogen or hydrogen-generating compounds, not provided for in a single one of groups C10G45/02, C10G45/32, C10G45/44, C10G45/58 or C10G47/00
    • C10G49/22—Separation of effluents
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2311/00—Details relating to membrane separation process operations and control
    • B01D2311/04—Specific process operations in the feed stream; Feed pretreatment
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2311/00—Details relating to membrane separation process operations and control
    • B01D2311/06—Specific process operations in the permeate stream
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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    • B01J23/16—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
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    • B01J23/16—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
    • B01J23/24—Chromium, molybdenum or tungsten
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    • B—PERFORMING OPERATIONS; TRANSPORTING
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    • B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
    • B01J23/74—Iron group metals
    • B01J23/755—Nickel
    • 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
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    • C—CHEMISTRY; METALLURGY
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    • C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B3/00—Extraction of metal compounds from ores or concentrates by wet processes
    • C22B3/20—Treatment or purification of solutions, e.g. obtained by leaching
    • C22B3/22—Treatment or purification of solutions, e.g. obtained by leaching by physical processes, e.g. by filtration, by magnetic means, or by thermal decomposition
    • C—CHEMISTRY; METALLURGY
    • C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Organic Chemistry (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Materials Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • General Chemical & Material Sciences (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Abstract

L'invention concerne un procédé pour valoriser du pétrole lourd et le convertir en produits d'hydrocarbures à point d'ébullition bas. Le procédé utilise un catalyseur en suspension comprenant des particules de catalyseur ayant une taille moyenne de particule s'échelonnant entre 1 et 20 microns. Dans le procédé de valorisation, le catalyseur en suspension usé dans le pétrole lourd est généré en tant que flux d'effluent. Dans un aspect de l'invention, le procédé comprend en outre la récupération du catalyseur usé par la séparation du pétrole lourd et des particules de catalyseur en suspension. Dans un mode de réalisation, le catalyseur en suspension dans le pétrole lourd est combiné avec du solvant pour former un flux combiné suspension-solvant. Le flux combiné suspension-solvant est filtré dans une zone de déshuilage par l'intermédiaire d'une filtration sur membrane. Les hydrocarbures, à savoir, le solvant et le pétrole lourd résiduel, peuvent être ultérieurement séparés des particules de catalyseur dans une zone de séchage. Les métaux de valeur peuvent être récupérés à partir des particules de catalyseur afin d'être réutilisés ultérieurement dans une unité de synthèse de catalyseur, en générant un catalyseur en suspension frais.
PCT/US2008/087682 2007-12-20 2008-12-19 Procédé de valorisation du pétrole lourd comprenant la récupération de catalyseur usé Ceased WO2009086107A2 (fr)

Priority Applications (3)

Application Number Priority Date Filing Date Title
BRPI0821358-5A BRPI0821358A2 (pt) 2007-12-20 2008-12-19 Sistema e processo para separar óleo pesado das partículas de catalisador, sistema para separar hidrocarbonetos, processo para separar óleo pesado dos particulados do catalisador, processo para remover hidrocarbonetos, e, processo para beneficiar uma carga de alimentação de óleo pesado.
CA2709072A CA2709072C (fr) 2007-12-20 2008-12-19 Procede de valorisation du petrole lourd comprenant la recuperation de catalyseur use
CN2008801251442A CN101918516B (zh) 2007-12-20 2008-12-19 包括废催化剂回收的重油提质方法

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
US12/004,014 2007-12-20
US12/004,014 US8722556B2 (en) 2007-12-20 2007-12-20 Recovery of slurry unsupported catalyst
US12/004,015 US8765622B2 (en) 2007-12-20 2007-12-20 Recovery of slurry unsupported catalyst
US12/004,015 2007-12-20

Publications (2)

Publication Number Publication Date
WO2009086107A2 WO2009086107A2 (fr) 2009-07-09
WO2009086107A3 true WO2009086107A3 (fr) 2009-09-24

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Application Number Title Priority Date Filing Date
PCT/US2008/087682 Ceased WO2009086107A2 (fr) 2007-12-20 2008-12-19 Procédé de valorisation du pétrole lourd comprenant la récupération de catalyseur usé

Country Status (5)

Country Link
KR (1) KR101584200B1 (fr)
CN (1) CN101918516B (fr)
BR (1) BRPI0821358A2 (fr)
CA (4) CA2943442C (fr)
WO (1) WO2009086107A2 (fr)

Families Citing this family (18)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102413908B (zh) 2009-04-29 2015-09-23 巴斯夫欧洲公司 借助膜过滤调节催化剂的方法
CN201793528U (zh) * 2010-05-27 2011-04-13 北京中天元环境工程有限责任公司 一种催化裂化油浆过滤设备
US8809222B2 (en) * 2010-12-30 2014-08-19 Chevron U.S.A. Inc. Hydroprocessing catalysts and methods for making thereof
FR2980377B1 (fr) * 2011-09-22 2013-10-04 Total Raffinage Marketing Procede de regeneration d'un catalyseur enzymatique
CN103663624B (zh) * 2012-09-14 2015-12-16 浙江中凯瑞普环境工程股份有限公司 一种油田回注水的精制方法
CN105854378B (zh) * 2015-01-23 2018-11-02 广西泓达生物能源科技有限公司 催化裂化油浆中残留催化剂颗粒分离设备
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CN110841349B (zh) * 2019-11-26 2024-06-18 中国成达工程有限公司 一种新型byd废催化剂处理系统
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CN113680300A (zh) * 2021-08-25 2021-11-23 西南石油大学 一种稠油降黏装置
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CA3212718A1 (fr) 2009-07-09
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CA2943442A1 (fr) 2009-07-09
CA2943442C (fr) 2020-09-15
CA2709072C (fr) 2016-11-29
CN101918516B (zh) 2013-06-12
WO2009086107A2 (fr) 2009-07-09
CN101918516A (zh) 2010-12-15
CA3089421A1 (fr) 2009-07-09
KR20100106484A (ko) 2010-10-01
BRPI0821358A2 (pt) 2015-06-16

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