ES372921A1 - Conversion and desulfurization of hydrocarbonaceous black oils - Google Patents

Conversion and desulfurization of hydrocarbonaceous black oils

Info

Publication number
ES372921A1
ES372921A1 ES372921A ES372921A ES372921A1 ES 372921 A1 ES372921 A1 ES 372921A1 ES 372921 A ES372921 A ES 372921A ES 372921 A ES372921 A ES 372921A ES 372921 A1 ES372921 A1 ES 372921A1
Authority
ES
Spain
Prior art keywords
zone
reaction zone
liquid phase
catalytic reaction
originate
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
ES372921A
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.)
Universal Oil Products Co
Original Assignee
Universal Oil Products Co
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 Universal Oil Products Co filed Critical Universal Oil Products Co
Publication of ES372921A1 publication Critical patent/ES372921A1/en
Expired legal-status Critical Current

Links

Classifications

    • 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
    • C10G69/00Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one other conversion process
    • C10G69/02Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one other conversion process plural serial stages only
    • C10G69/06Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one other conversion process plural serial stages only including at least one step of thermal cracking in the absence of hydrogen
    • 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
    • C10G49/00Treatment 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
    • C10G49/007Treatment 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 in the presence of hydrogen from a special source or of a special composition or having been purified by a special treatment

Abstract

A process for the conversion and desulfurization of a hydrocarbon, sulphidated filler material of which at least about 10.0% boils above a temperature of about 566ºC to give low-boiling hydrocarbon products, the process comprising : a) heating said charge to a temperature between approximately 260 and 399ºC; b) contacting said heated filler material with a catalytic compound in a catalytic reaction zone, and reacting therein said filler material with hydrogen at a pressure greater than 68 gauge atmospheres; c) separating the resulting effluent from the reaction zone in a first separation zone, at substantially the same pressure as that maintained in said catalytic reaction zone, to originate a first vapor phase and a first liquid phase; d) separating the first vapor phase in the second separation zone urn, at substantially the same pressure as that maintained in said first separation zone, to originate a second hydrogen-rich vapor phase and a second liquid phase; e) fractionating at least a portion of said first liquid phase in a non-catalytic reaction zone; f) introducing the effluent resulting from said non-catalytic reaction zone into a fractionation zone; g) extracting from said fractionation zone a heavy hydrocarbon stream boiling substantially above a temperature of about 343ºC, and introducing said stream into a third separation zone; and h) separating said heavy hydrocarbon stream therein, at a reduced pressure comprised between a sub-atmospheric pressure and about 3.4 gauge atmospheres, to originate a third liquid phase containing distilled hydrocarbons and a residue concentrate. (Machine-translation by Google Translate, not legally binding)
ES372921A 1968-10-28 1969-10-27 Conversion and desulfurization of hydrocarbonaceous black oils Expired ES372921A1 (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US77124868A 1968-10-28 1968-10-28

Publications (1)

Publication Number Publication Date
ES372921A1 true ES372921A1 (en) 1971-11-16

Family

ID=25091198

Family Applications (1)

Application Number Title Priority Date Filing Date
ES372921A Expired ES372921A1 (en) 1968-10-28 1969-10-27 Conversion and desulfurization of hydrocarbonaceous black oils

Country Status (14)

Country Link
US (1) US3594309A (en)
JP (1) JPS4830441B1 (en)
AT (1) AT303941B (en)
BR (1) BR6913678D0 (en)
CS (1) CS166719B2 (en)
DK (1) DK133474B (en)
ES (1) ES372921A1 (en)
FR (1) FR2021705A1 (en)
GB (1) GB1276864A (en)
NL (1) NL6916218A (en)
NO (1) NO126919B (en)
OA (1) OA03157A (en)
SE (1) SE369197B (en)
SU (1) SU374838A3 (en)

Families Citing this family (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4606812A (en) * 1980-04-15 1986-08-19 Chemroll Enterprises, Inc. Hydrotreating of carbonaceous materials
US4446004A (en) * 1982-12-23 1984-05-01 Mobil Oil Corporation Process for upgrading vacuum resids to premium liquid products
US4604185A (en) * 1985-07-02 1986-08-05 Conoco Inc. Co-processing of straight run vacuum resid and cracked residua
US4661238A (en) * 1985-09-05 1987-04-28 Uop Inc. Combination process for the conversion of a distillate hydrocarbon to maximize middle distillate production
US4721557A (en) * 1986-10-08 1988-01-26 Uop Inc. Combination process for the conversion of a residual asphaltene-containing hydrocarbonaceous stream to maximize middle distillate production
US4715947A (en) * 1986-11-24 1987-12-29 Uop Inc. Combination process for the conversion of a residual asphaltene-containing hydrocarbonaceous stream to maximize middle distillate production
US4792390A (en) * 1987-09-21 1988-12-20 Uop Inc. Combination process for the conversion of a distillate hydrocarbon to produce middle distillate product
US4961839A (en) * 1988-05-23 1990-10-09 Uop High conversion hydrocracking process
US7938953B2 (en) * 2008-05-20 2011-05-10 Institute Francais Du Petrole Selective heavy gas oil recycle for optimal integration of heavy oil conversion and vacuum gas oil treating

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR659583A (en) * 1927-09-01 1929-07-01 Ig Farbenindustrie Ag Process for the production of high value hydrocarbons
FR1313068A (en) * 1959-06-04 1962-12-28 Inst Francais Du Petrole Continuous process of hydrotreating petroleum products
FR1386576A (en) * 1963-07-02 1965-01-22 Gulf Research Development Co Process for treating a mixture of hydrocarbons
US3324028A (en) * 1964-04-22 1967-06-06 Gulf Research Development Co Preparation of low sulfur content heavy fuel oils
US3371029A (en) * 1966-11-30 1968-02-27 Universal Oil Prod Co Mixed-phase conversion product separation process
US3371030A (en) * 1966-12-30 1968-02-27 Universal Oil Prod Co Black oil conversion product separation process

Also Published As

Publication number Publication date
OA03157A (en) 1970-12-15
NO126919B (en) 1973-04-09
DE1954002A1 (en) 1970-05-21
BR6913678D0 (en) 1973-01-23
AT303941B (en) 1972-12-11
FR2021705A1 (en) 1970-07-24
DK133474C (en) 1976-11-01
NL6916218A (en) 1970-05-01
DK133474B (en) 1976-05-24
US3594309A (en) 1971-07-20
CS166719B2 (en) 1976-03-29
SE369197B (en) 1974-08-12
JPS4830441B1 (en) 1973-09-20
SU374838A3 (en) 1973-03-20
GB1276864A (en) 1972-06-07

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