WO2002100980A3 - Two-stage heavy feed hpc process - Google Patents

Two-stage heavy feed hpc process Download PDF

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Publication number
WO2002100980A3
WO2002100980A3 PCT/EP2002/006665 EP0206665W WO02100980A3 WO 2002100980 A3 WO2002100980 A3 WO 2002100980A3 EP 0206665 W EP0206665 W EP 0206665W WO 02100980 A3 WO02100980 A3 WO 02100980A3
Authority
WO
WIPO (PCT)
Prior art keywords
catalyst
pore volume
total pore
pores
diameter
Prior art date
Application number
PCT/EP2002/006665
Other languages
French (fr)
Other versions
WO2002100980A2 (en
Inventor
Satoshi Abe
Katsuhisa Fujita
Original Assignee
Nippon Ketjen Co Ltd
Akzo Nobel Nv
Satoshi Abe
Katsuhisa Fujita
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 Nippon Ketjen Co Ltd, Akzo Nobel Nv, Satoshi Abe, Katsuhisa Fujita filed Critical Nippon Ketjen Co Ltd
Priority to EP02748792A priority Critical patent/EP1392800B1/en
Priority to CA2449637A priority patent/CA2449637C/en
Priority to US10/480,176 priority patent/US7476309B2/en
Priority to PL367266A priority patent/PL196409B1/en
Priority to AU2002319243A priority patent/AU2002319243A1/en
Priority to SK1498-2003A priority patent/SK286656B6/en
Publication of WO2002100980A2 publication Critical patent/WO2002100980A2/en
Publication of WO2002100980A3 publication Critical patent/WO2002100980A3/en

Links

Classifications

    • B01J35/60—
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • 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
    • B01J23/76—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
    • B01J23/84—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36 with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
    • B01J23/85—Chromium, molybdenum or tungsten
    • B01J35/19—
    • 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
    • C10G65/00—Treatment of hydrocarbon oils by two or more hydrotreatment processes only
    • C10G65/02—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial 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
    • C10G65/00—Treatment of hydrocarbon oils by two or more hydrotreatment processes only
    • C10G65/02—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only
    • C10G65/10—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only including only cracking steps
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J21/00—Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
    • B01J21/02—Boron or aluminium; Oxides or hydroxides thereof
    • B01J21/04—Alumina
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J21/00—Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
    • B01J21/12—Silica and alumina
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • 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
    • B01J23/76—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
    • B01J23/84—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36 with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
    • B01J23/85—Chromium, molybdenum or tungsten
    • B01J23/88—Molybdenum
    • B01J23/883—Molybdenum and nickel
    • B01J35/615—
    • B01J35/635—
    • B01J35/66—
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/0009—Use of binding agents; Moulding; Pressing; Powdering; Granulating; Addition of materials ameliorating the mechanical properties of the product catalyst
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/02—Impregnation, coating or precipitation
    • B01J37/0201—Impregnation
    • 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
    • C10G2300/202—Heteroatoms content, i.e. S, N, O, P
    • 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

Landscapes

  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Materials Engineering (AREA)
  • Catalysts (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Abstract

The present invention pertains to a method for hydroprocessing a heavy hydrocarbon oil, comprising bringing a heavy hydrocarbon oil into contact with hydroprocessing catalyst I in the presence of hydrogen in a first stage, after which the effluent of the first stage is contacted in whole or in part with hydroprocessing catalyst II in the presence of hydrogen, wherein catalyst I comprises 7 to 20 wt.% of a Group VIB metal component, calculated as trioxide on the weight of the catalyst, and 0.5 to 6 wt.% of a Group VIII metal component, calculated as oxide on the weight of the catalyst, on a porous inorganic carrier, said catalyst having a specific surface area of at least 100 m2/g, a total pore volume of at least 0,55 ml/g, at least 50 % of the total pore volume in pores with a diameter of at least 20 nm (200 Å), and 10-30% of the total pore volume in pores with a diameter of at least 200 nm (2000 Å), and catalyst II comprises 7 to 20 wt.% of a group VIB metal component, calculated as trioxide on the weight of the catalyst, and 0.5 to 6 wt.% of a Group VIII metal component, calculated as oxide on the weight of the catalyst, on a porous inorganic carrier, said catalyst having a specific surface area of at least 100 m2/g, a total pore volume of at least 0.55 ml/g, at least 75% of the total pore volume in pores with a diameter of 10-120 nm (100-1200 Å), 0-2% of the total pore volume in pores with a diameter of at least 400 nm (4000 Å), and 0-1% of the total pore volume in pores with a diameter of at least 1000 nm (10000 Å). The method according to the invention combined efficient contaminant removal with high cracking rate and low sediment formation. The invention also pertains to the combination of catalysts.
PCT/EP2002/006665 2001-06-08 2002-06-10 Two-stage heavy feed hpc process WO2002100980A2 (en)

Priority Applications (6)

Application Number Priority Date Filing Date Title
EP02748792A EP1392800B1 (en) 2001-06-08 2002-06-10 Two-stage heavy feed hpc process
CA2449637A CA2449637C (en) 2001-06-08 2002-06-10 Two-stage heavy feed hpc process
US10/480,176 US7476309B2 (en) 2001-06-08 2002-06-10 Two-stage heavy feed hpc process
PL367266A PL196409B1 (en) 2001-06-08 2002-06-10 Two-stage heavy feed hpc process
AU2002319243A AU2002319243A1 (en) 2001-06-08 2002-06-10 Two-stage heavy feed hpc process
SK1498-2003A SK286656B6 (en) 2001-06-08 2002-06-10 Two-stage heavy feed HPC process

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
JP2001-174073 2001-06-08
JP2001174073A JP4773634B2 (en) 2001-06-08 2001-06-08 Two-stage hydroprocessing method for heavy hydrocarbon oil

Publications (2)

Publication Number Publication Date
WO2002100980A2 WO2002100980A2 (en) 2002-12-19
WO2002100980A3 true WO2002100980A3 (en) 2003-04-10

Family

ID=19015411

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/EP2002/006665 WO2002100980A2 (en) 2001-06-08 2002-06-10 Two-stage heavy feed hpc process

Country Status (8)

Country Link
US (1) US7476309B2 (en)
EP (1) EP1392800B1 (en)
JP (1) JP4773634B2 (en)
AU (1) AU2002319243A1 (en)
CA (1) CA2449637C (en)
PL (1) PL196409B1 (en)
SK (1) SK286656B6 (en)
WO (1) WO2002100980A2 (en)

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FR2846574B1 (en) * 2002-10-30 2006-05-26 Inst Francais Du Petrole CATALYST AND PROCESS FOR HYDROCRACKING HYDROCARBON LOADS
JP4646500B2 (en) * 2003-05-20 2011-03-09 独立行政法人産業技術総合研究所 Hydrotreating catalyst using impregnation solution for hydrotreating catalyst
JP5051868B2 (en) * 2003-07-09 2012-10-17 インステイチユート メキシカノ デル ペトロレオ Method of catalytic hydrotreating heavy petroleum hydrocarbons
US7410565B1 (en) * 2004-12-17 2008-08-12 Uop Llc Multi-catalyst selection for chlorided reforming catalyst
US7615142B2 (en) * 2006-08-31 2009-11-10 Headwaters Technology Innovation, Llc Expanded bed reactor system and method for hydroprocessing wax produced by Fischer-Tropsch reaction and contaminated with solids
US8480881B2 (en) 2009-06-11 2013-07-09 Board Of Regents, The University Of Texas System Synthesis of acidic silica to upgrade heavy feeds
CN103059935B (en) * 2011-10-20 2014-12-31 中国石油化工股份有限公司 Fixed bed hydrotreating method of heavy oil
CN103059936B (en) * 2011-10-20 2014-10-29 中国石油化工股份有限公司 Hydrotreating method of heavy oil
CN103374394B (en) * 2012-04-19 2015-02-25 中国石油化工股份有限公司 Grading loading method of catalyst and application of grading loading method, and hydrogenation treatment method of heavy oils
CN103773451B (en) * 2012-10-19 2015-08-26 中国石油化工股份有限公司 A kind of fixed bed residual hydrogenation method
US9650312B2 (en) 2013-03-14 2017-05-16 Lummus Technology Inc. Integration of residue hydrocracking and hydrotreating
US10208261B2 (en) * 2014-02-12 2019-02-19 Lummus Technology Inc. Processing vacuum residuum and vacuum gas oil in ebullated bed reactor systems
CN105985805B (en) * 2015-01-29 2018-07-13 中国石油天然气股份有限公司 A kind of catalyst for hydroprocessing of heavy oil grading loading method
US20180230389A1 (en) 2017-02-12 2018-08-16 Magēmā Technology, LLC Multi-Stage Process and Device for Reducing Environmental Contaminates in Heavy Marine Fuel Oil
US11788017B2 (en) 2017-02-12 2023-10-17 Magëmã Technology LLC Multi-stage process and device for reducing environmental contaminants in heavy marine fuel oil
US10604709B2 (en) 2017-02-12 2020-03-31 Magēmā Technology LLC Multi-stage device and process for production of a low sulfur heavy marine fuel oil from distressed heavy fuel oil materials

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US4830736A (en) * 1986-07-28 1989-05-16 Chevron Research Company Graded catalyst system for removal of calcium and sodium from a hydrocarbon feedstock
US4789462A (en) * 1986-09-29 1988-12-06 Chevron Research Company Reverse-graded catalyst systems for hydrodemetalation and hydrodesulfurization
US5744025A (en) * 1997-02-28 1998-04-28 Shell Oil Company Process for hydrotreating metal-contaminated hydrocarbonaceous feedstock

Also Published As

Publication number Publication date
AU2002319243A1 (en) 2002-12-23
EP1392800B1 (en) 2006-08-16
PL367266A1 (en) 2005-02-21
PL196409B1 (en) 2007-12-31
JP2002363576A (en) 2002-12-18
SK14982003A3 (en) 2004-06-08
EP1392800A2 (en) 2004-03-03
US7476309B2 (en) 2009-01-13
JP4773634B2 (en) 2011-09-14
CA2449637C (en) 2012-07-31
SK286656B6 (en) 2009-03-05
WO2002100980A2 (en) 2002-12-19
US20040209771A1 (en) 2004-10-21
CA2449637A1 (en) 2002-12-19

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