ES361321A1 - Improvements in or relating to Desulfurization - Google Patents

Improvements in or relating to Desulfurization

Info

Publication number
ES361321A1
ES361321A1 ES361321A ES361321A ES361321A1 ES 361321 A1 ES361321 A1 ES 361321A1 ES 361321 A ES361321 A ES 361321A ES 361321 A ES361321 A ES 361321A ES 361321 A1 ES361321 A1 ES 361321A1
Authority
ES
Spain
Prior art keywords
catalyst
surface area
pore volume
silica content
desulfurization
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.)
Expired
Application number
ES361321A
Other languages
Spanish (es)
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.)
Texaco Development Corp
Original Assignee
Texaco Development Corp
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 Texaco Development Corp filed Critical Texaco Development Corp
Publication of ES361321A1 publication Critical patent/ES361321A1/en
Expired legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/70Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
    • B01J23/76Catalysts 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
    • B01J23/84Catalysts 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
    • B01J23/85Chromium, molybdenum or tungsten
    • 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
    • C10G2300/00Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/10Feedstock materials
    • C10G2300/107Atmospheric residues having a boiling point of at least about 538 °C

Landscapes

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

Abstract

Petroleum fractions having a Conradson Carbon Residue of at least 1% b.w. are hydrodesulphurized at elevated pressure and temperature over a supported catalyst comprising a compound of a Group VI metal, e.g. Mo or W, and one of Fe, Co or Ni, the catalyst having a surface area of at least 250 m2/g, a pore volume of at least 0À6 c.c./g. and a silica content of at least 2% b.w. of the catalyst composite. The preferred surface area is in the range 300 to 400 m2/g, with a maximum of 800 m2/g, and the pore volume may be up to 1À0 c.c./g. and the silica content may be up to 30% b.w. The catalyst support may include alumina, zirconia or magnesia. Reaction conditions are conventional. Feeds treated are typically crudes and residuals, including tar sand oil and shale oil.
ES361321A 1967-12-12 1968-12-11 Improvements in or relating to Desulfurization Expired ES361321A1 (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US68982567A 1967-12-12 1967-12-12

Publications (1)

Publication Number Publication Date
ES361321A1 true ES361321A1 (en) 1970-08-16

Family

ID=24770020

Family Applications (1)

Application Number Title Priority Date Filing Date
ES361321A Expired ES361321A1 (en) 1967-12-12 1968-12-11 Improvements in or relating to Desulfurization

Country Status (9)

Country Link
BE (1) BE725291A (en)
BR (1) BR6804766D0 (en)
DE (1) DE1814043C3 (en)
DK (1) DK131685C (en)
ES (1) ES361321A1 (en)
FR (1) FR1594411A (en)
GB (1) GB1194960A (en)
NL (1) NL159019B (en)
SE (1) SE371649B (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
NL167464C (en) * 1970-07-14 1981-12-16 Shell Int Research PROCESS FOR THE CATALYTICALLY HYDRATING DEFUSIONING OF RESIDUAL HYDROCARBON OILS.
FR2097016B1 (en) * 1970-07-27 1973-05-25 Inst Francais Du Petrole

Also Published As

Publication number Publication date
DK131685C (en) 1976-01-19
BR6804766D0 (en) 1973-01-04
DK131685B (en) 1975-08-18
SE371649B (en) 1974-11-25
NL6817714A (en) 1969-06-16
DE1814043A1 (en) 1969-07-03
BE725291A (en) 1969-06-11
DE1814043C3 (en) 1979-11-15
NL159019B (en) 1979-01-15
DE1814043B2 (en) 1979-03-01
GB1194960A (en) 1970-06-17
FR1594411A (en) 1970-06-01

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