CA2929190C - A process for the catalytic conversion of micro carbon residue content of heavy hydrocarbon feedstocks and a low surface area catalyst composition for use therein - Google Patents

A process for the catalytic conversion of micro carbon residue content of heavy hydrocarbon feedstocks and a low surface area catalyst composition for use therein Download PDF

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Publication number
CA2929190C
CA2929190C CA2929190A CA2929190A CA2929190C CA 2929190 C CA2929190 C CA 2929190C CA 2929190 A CA2929190 A CA 2929190A CA 2929190 A CA2929190 A CA 2929190A CA 2929190 C CA2929190 C CA 2929190C
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Prior art keywords
catalyst
range
pores
pore volume
total
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CA2929190A
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English (en)
French (fr)
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CA2929190A1 (en
Inventor
Josiane Marie-Rose Ginestra
David Edward Sherwood
David Andrew Komar
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Shell Internationale Research Maatschappij BV
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Shell Internationale Research Maatschappij BV
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Classifications

    • 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
    • B01J27/00—Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
    • B01J27/14—Phosphorus; Compounds thereof
    • B01J27/186—Phosphorus; Compounds thereof with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
    • B01J27/188—Phosphorus; Compounds thereof with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium with chromium, molybdenum, tungsten or polonium
    • B01J27/19—Molybdenum
    • 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
    • B01J35/00—Catalysts, in general, characterised by their form or physical properties
    • B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
    • B01J35/61—Surface area
    • B01J35/615—100-500 m2/g
    • 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
    • B01J35/00—Catalysts, in general, characterised by their form or physical properties
    • B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
    • B01J35/64—Pore diameter
    • B01J35/647—2-50 nm
    • 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
    • B01J35/00—Catalysts, in general, characterised by their form or physical properties
    • B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
    • B01J35/66—Pore distribution
    • 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
    • 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
    • C10G45/02—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing
    • C10G45/04—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing characterised by the catalyst used
    • C10G45/06—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing characterised by the catalyst used containing nickel or cobalt metal, or compounds thereof
    • C10G45/08—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing characterised by the catalyst used containing nickel or cobalt metal, or compounds thereof in combination with chromium, molybdenum, or tungsten metals, or compounds thereof
    • 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
    • C10G45/60—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 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
    • C10G47/00—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions
    • C10G47/02—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions characterised by the catalyst used
    • C10G47/04—Oxides
    • 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

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Materials Engineering (AREA)
  • General Chemical & Material Sciences (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Catalysts (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Nanotechnology (AREA)
CA2929190A 2013-11-25 2014-11-20 A process for the catalytic conversion of micro carbon residue content of heavy hydrocarbon feedstocks and a low surface area catalyst composition for use therein Active CA2929190C (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
US201361908334P 2013-11-25 2013-11-25
US61/908,334 2013-11-25
PCT/US2014/066493 WO2015077390A1 (en) 2013-11-25 2014-11-20 A process for the catalytic conversion of micro carbon residue content of heavy hydrocarbon feedstocks and a low surface area catalyst composition for use therein

Publications (2)

Publication Number Publication Date
CA2929190A1 CA2929190A1 (en) 2015-05-28
CA2929190C true CA2929190C (en) 2021-10-12

Family

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Family Applications (1)

Application Number Title Priority Date Filing Date
CA2929190A Active CA2929190C (en) 2013-11-25 2014-11-20 A process for the catalytic conversion of micro carbon residue content of heavy hydrocarbon feedstocks and a low surface area catalyst composition for use therein

Country Status (9)

Country Link
US (2) US10507459B2 (https=)
EP (1) EP3074486B1 (https=)
JP (1) JP6553030B2 (https=)
KR (1) KR102360689B1 (https=)
CN (1) CN105745309B (https=)
CA (1) CA2929190C (https=)
DK (1) DK3074486T3 (https=)
TW (1) TWI651406B (https=)
WO (1) WO2015077390A1 (https=)

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MX2018008283A (es) * 2016-01-06 2019-05-13 Oren Tech Llc Transportador con sistema integrado de recoleccion de polvo.
US12071592B2 (en) 2017-02-12 2024-08-27 Magēmā Technology LLC Multi-stage process and device utilizing structured catalyst beds and reactive distillation for the production of a low sulfur heavy marine fuel oil
US12281266B2 (en) 2017-02-12 2025-04-22 Magẽmã Technology LLC Heavy marine fuel oil composition
US12025435B2 (en) 2017-02-12 2024-07-02 Magēmã Technology LLC Multi-stage device and process for production of a low sulfur heavy marine fuel oil
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
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
US12559689B2 (en) 2017-02-12 2026-02-24 Magēmā Technology LLC Multi-stage process and device for treatment heavy marine fuel and resultant composition and the removal of detrimental solids
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
WO2022150366A1 (en) * 2021-01-08 2022-07-14 Advanced Refining Technologies Llc High activity hydrotreating catalysts and processes using same

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US582742A (en) 1897-05-18 John joseph iioratst
US5827421A (en) * 1992-04-20 1998-10-27 Texaco Inc Hydroconversion process employing catalyst with specified pore size distribution and no added silica
US5397456A (en) 1993-02-19 1995-03-14 Texaco Inc. Hydroconversion process employing catalyst with specified pore size distribution
US5928499A (en) * 1993-10-01 1999-07-27 Texaco Inc Hydroconversion process employing catalyst with specified pore size distribution, median pore diameter by surface area, and pore mode by volume
US5514273A (en) 1993-10-01 1996-05-07 Texaco Inc. Hydroconversion process employing catalyst with specified pore size distribution
US5468371A (en) * 1994-04-11 1995-11-21 Texaco Inc. Catalyst for residual conversion demonstrating reduced toluene insolubles
US5968348A (en) * 1994-05-16 1999-10-19 Texaco Inc. Hydroconversion process employing a phosphorus loaded NiMo catalyst with specified pore size distribution
FI970356L (fi) 1994-07-29 1997-01-28 Chevron Usa Inc Pienen makrohuokosmäärän sisältävä tislausjäännöksen konversiokatalyytti
US6387248B2 (en) * 1997-11-06 2002-05-14 Texaco Inc. Method of preparing a catalyst for use in the hydrotreating of high boiling hydrocarbon feedstocks
US6338265B1 (en) * 2000-03-09 2002-01-15 Jimmy Raider Grigg Device for straightening aluminum fins
WO2004052534A1 (en) 2002-12-06 2004-06-24 Albemarle Netherlands B.V. Heavy feed hpc process using a mixture of catalysts
RU2376059C2 (ru) 2003-09-17 2009-12-20 Шелл Интернэшнл Рисерч Маатсхаппий Б.В. Способ и катализатор гидроконверсии тяжелого углеводородного исходного сырья
AU2005265004A1 (en) * 2004-06-17 2006-01-26 Exxonmobil Research And Engineering Company Catalyst combination and two-step hydroprocessing method for heavy hydrocarbon oil
CN100510022C (zh) * 2005-09-28 2009-07-08 中国石油化工股份有限公司 一种多产优质柴油的低氢耗加氢方法
BRPI0714518B8 (pt) 2006-08-03 2017-05-16 Shell Int Research método para produzir um catalisador altamente estável para hidrodessulfurização de hidrocarbonetos pesados e processo para dessulfurizar um suprimento de hidrocarbonetos pesados
US8372268B2 (en) 2009-03-24 2013-02-12 Shell Oil Company High surface area composition for use in the catalytic hydroconversion of a heavy hydrocarbon feedstock, a method making such composition and its use

Also Published As

Publication number Publication date
KR102360689B1 (ko) 2022-02-08
US10507459B2 (en) 2019-12-17
DK3074486T3 (en) 2018-10-08
US11344865B2 (en) 2022-05-31
US20150144531A1 (en) 2015-05-28
TWI651406B (zh) 2019-02-21
EP3074486A1 (en) 2016-10-05
EP3074486B1 (en) 2018-06-27
WO2015077390A1 (en) 2015-05-28
JP6553030B2 (ja) 2019-07-31
TW201542802A (zh) 2015-11-16
US20200055033A1 (en) 2020-02-20
KR20160090314A (ko) 2016-07-29
CN105745309B (zh) 2019-04-05
JP2016539222A (ja) 2016-12-15
CN105745309A (zh) 2016-07-06
CA2929190A1 (en) 2015-05-28

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