ZA981604B - Process for hydrotreating metal-contaminated hydrocarbonaceous feedstocks - Google Patents

Process for hydrotreating metal-contaminated hydrocarbonaceous feedstocks

Info

Publication number
ZA981604B
ZA981604B ZA981604A ZA981604A ZA981604B ZA 981604 B ZA981604 B ZA 981604B ZA 981604 A ZA981604 A ZA 981604A ZA 981604 A ZA981604 A ZA 981604A ZA 981604 B ZA981604 B ZA 981604B
Authority
ZA
South Africa
Prior art keywords
hydrocarbonaceous feedstocks
contaminated
hydrotreating
hydrotreating metal
metal
Prior art date
Application number
ZA981604A
Other languages
English (en)
Inventor
Opinder Kishan Bhan
Andries Quirin Maria Boon
Constantinus Johannes Ja Ouden
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 ZA981604B publication Critical patent/ZA981604B/xx

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
    • C10G45/02—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
    • 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
    • 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
    • B01J35/63—Pore volume
    • B01J35/635—0.5-1.0 ml/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
    • 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
    • C10G2300/40—Characteristics of the process deviating from typical ways of processing
    • C10G2300/4087—Catalytic distillation

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Materials Engineering (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • General Chemical & Material Sciences (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Catalysts (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
ZA981604A 1997-02-28 1998-02-26 Process for hydrotreating metal-contaminated hydrocarbonaceous feedstocks ZA981604B (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US08/808,597 US5744025A (en) 1997-02-28 1997-02-28 Process for hydrotreating metal-contaminated hydrocarbonaceous feedstock

Publications (1)

Publication Number Publication Date
ZA981604B true ZA981604B (en) 1999-02-19

Family

ID=25199220

Family Applications (1)

Application Number Title Priority Date Filing Date
ZA981604A ZA981604B (en) 1997-02-28 1998-02-26 Process for hydrotreating metal-contaminated hydrocarbonaceous feedstocks

Country Status (8)

Country Link
US (1) US5744025A (xx)
EP (1) EP0861881A1 (xx)
JP (1) JPH10251666A (xx)
KR (1) KR19980071763A (xx)
CN (1) CN1093164C (xx)
CA (1) CA2230605A1 (xx)
TW (1) TW426727B (xx)
ZA (1) ZA981604B (xx)

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US7569136B2 (en) 1997-06-24 2009-08-04 Ackerson Michael D Control system method and apparatus for two phase hydroprocessing
US7291257B2 (en) * 1997-06-24 2007-11-06 Process Dynamics, Inc. Two phase hydroprocessing
AU755160B2 (en) 1997-06-24 2002-12-05 E.I. Du Pont De Nemours And Company Two phase hydroprocessing
US6918442B2 (en) 2001-04-24 2005-07-19 Shell Oil Company In situ thermal processing of an oil shale formation in a reducing environment
JP4773634B2 (ja) * 2001-06-08 2011-09-14 日本ケッチェン株式会社 重質炭化水素油の２段階水素化処理方法
CA2462957C (en) 2001-10-24 2011-03-01 Shell Canada Limited In situ thermal processing of a hydrocarbon containing formation and upgrading of produced fluids prior to further treatment
JP2004010857A (ja) * 2002-06-11 2004-01-15 Nippon Kecchen Kk 重質炭化水素油の水素化処理方法
JP4798685B2 (ja) * 2002-09-24 2011-10-19 Ｊｘ日鉱日石エネルギー株式会社 石油系重質油の脱金属方法
US7745369B2 (en) * 2003-12-19 2010-06-29 Shell Oil Company Method and catalyst for producing a crude product with minimal hydrogen uptake
US8025794B2 (en) * 2003-12-19 2011-09-27 Shell Oil Company Systems, methods, and catalysts for producing a crude product
NL1027751C2 (nl) 2003-12-19 2006-07-13 Shell Int Research Systemen, methoden en katalysatoren voor het produceren van een ruwe-oliehoudend product.
US20070000810A1 (en) * 2003-12-19 2007-01-04 Bhan Opinder K Method for producing a crude product with reduced tan
US20070000808A1 (en) * 2003-12-19 2007-01-04 Bhan Opinder K Method and catalyst for producing a crude product having selected properties
US7416653B2 (en) * 2003-12-19 2008-08-26 Shell Oil Company Systems and methods of producing a crude product
US20070012595A1 (en) * 2003-12-19 2007-01-18 Brownscombe Thomas F Methods for producing a total product in the presence of sulfur
US20060289340A1 (en) * 2003-12-19 2006-12-28 Brownscombe Thomas F Methods for producing a total product in the presence of sulfur
TW200602591A (en) * 2004-07-08 2006-01-16 hong-yang Chen Gas supply device by gasifying burnable liquid
TWI415930B (zh) * 2005-04-06 2013-11-21 Shell Int Research 減少液態含烴原料總酸值（ｔａｎ）的方法
EP1874896A1 (en) * 2005-04-11 2008-01-09 Shell International Research Maatschappij B.V. Method and catalyst for producing a crude product having a reduced nitroge content
CN101166807A (zh) * 2005-04-11 2008-04-23 国际壳牌研究有限公司 生产原油产品的系统、方法和催化剂
US7918992B2 (en) * 2005-04-11 2011-04-05 Shell Oil Company Systems, methods, and catalysts for producing a crude product
WO2006110595A1 (en) * 2005-04-11 2006-10-19 Shell Internationale Research Maatschappij B.V. Method and catalyst for producing a crude product having a reduced nitrogen content
CA2604015C (en) * 2005-04-11 2014-02-18 Shell International Research Maatschappij B.V. Systems, methods, and catalysts for producing a crude product
WO2007050479A1 (en) 2005-10-24 2007-05-03 Shell Internationale Research Maatschappij B.V. Solution mining systems and methods for treating hydrocarbon containing formations
KR101440312B1 (ko) 2006-04-21 2014-09-15 쉘 인터내셔날 리써취 마트샤피지 비.브이. 고강도 합금
WO2007149923A2 (en) * 2006-06-22 2007-12-27 Shell Oil Company Method for producing a crude product with a long-life catalyst
EP2029698A1 (en) * 2006-06-22 2009-03-04 Shell Internationale Research Maatschappij B.V. Methods for producing a crude product from selected feed
WO2007149917A1 (en) * 2006-06-22 2007-12-27 Shell Oil Company Methods for producing a total product with selective hydrocarbon production
US7749374B2 (en) 2006-10-06 2010-07-06 Shell Oil Company Methods for producing a crude product
US7681647B2 (en) 2006-10-20 2010-03-23 Shell Oil Company Method of producing drive fluid in situ in tar sands formations
US8327681B2 (en) 2007-04-20 2012-12-11 Shell Oil Company Wellbore manufacturing processes for in situ heat treatment processes
US20090189617A1 (en) 2007-10-19 2009-07-30 David Burns Continuous subsurface heater temperature measurement
CN102344827B (zh) * 2010-08-05 2014-03-12 中国石油化工股份有限公司 一种催化裂化重油加氢方法
WO2012100068A2 (en) 2011-01-19 2012-07-26 Process Dynamics, Inc. Process for hydroprocessing of non-petroleum feestocks
CN103045302B (zh) * 2011-10-17 2015-02-18 中国石油化工股份有限公司 一种加氢处理催化剂的级配方法
CN103059929B (zh) * 2011-10-18 2015-07-01 中国石油化工股份有限公司 一种重质渣油的加氢处理方法
CN103725324B (zh) * 2013-12-27 2015-06-03 成都博晟能源科技有限公司 一种煤焦油低压脱金属的方法
TWI723904B (zh) 2020-06-18 2021-04-01 宏碁股份有限公司 輸入裝置的按壓結構

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US4657663A (en) * 1985-04-24 1987-04-14 Phillips Petroleum Company Hydrotreating process employing a three-stage catalyst system wherein a titanium compound is employed in the second stage
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Also Published As

Publication number Publication date
CN1093164C (zh) 2002-10-23
CN1197105A (zh) 1998-10-28
JPH10251666A (ja) 1998-09-22
EP0861881A1 (en) 1998-09-02
CA2230605A1 (en) 1998-08-28
US5744025A (en) 1998-04-28
TW426727B (en) 2001-03-21
KR19980071763A (ko) 1998-10-26

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