GB1221275A - Process for the convesion of a hydrocarbon oil containing residual material - Google Patents

Process for the convesion of a hydrocarbon oil containing residual material

Info

Publication number
GB1221275A
GB1221275A GB5169969A GB5169969A GB1221275A GB 1221275 A GB1221275 A GB 1221275A GB 5169969 A GB5169969 A GB 5169969A GB 5169969 A GB5169969 A GB 5169969A GB 1221275 A GB1221275 A GB 1221275A
Authority
GB
United Kingdom
Prior art keywords
fraction
boiling point
hydrocracking
stream
final boiling
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
GB5169969A
Inventor
Douglas Grant Mooney
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.)
Shell Internationale Research Maatschappij BV
Original Assignee
Shell Internationale Research Maatschappij BV
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 Internationale Research Maatschappij BV filed Critical Shell Internationale Research Maatschappij BV
Priority to GB5169969A priority Critical patent/GB1221275A/en
Priority to NL7006961A priority patent/NL166495C/en
Priority to JP9172270A priority patent/JPS511726B1/ja
Priority to FR7037830A priority patent/FR2065459B1/fr
Priority to DE19702051475 priority patent/DE2051475C2/en
Priority to CA096063A priority patent/CA927766A/en
Publication of GB1221275A publication Critical patent/GB1221275A/en
Expired legal-status Critical Current

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
    • 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
    • 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
    • C10G2300/10—Feedstock materials
    • C10G2300/107—Atmospheric residues having a boiling point of at least about 538 °C

Abstract

1,221,275. Hydrocracking; hydrorefining. SHELL INTERNATIONALE RESEARCH MAATSCHAPPIJ N.V. 22 Oct., 1969, No. 51699/69. Heading C5E. A hydrocarbon oil is treated by (1) catalytic hydrocracking at 5; (2) separating the effluent at 12 into (a) a fraction 14 having a final boiling point below 350‹ C.; (b) a fraction 28 with an initial boiling point between 180‹ and 350‹ C. and final boiling point between 450‹ and 550‹ C.; and (c) a fraction 13 with an initial boiling point between 450‹ and 550‹ C.; (3) catalytically hydrotreating at 18 the fractions of final boiling point between 180‹ and 350‹ C.; (4) catalytically hydrocracking the fraction (b) at 32; (5) separating the products from (3) and (4) at 27 into (d) a fraction 40 having a final boiling point between 150‹ and 180‹ C.; (e) a fraction 41 of initial boiling point between 150‹ and 180‹ C. and final boiling point between 230‹ and 290‹ C.; (f) a fraction 42 of initial boiling point between 230-290‹ C. and final boiling point up to 350‹ C.; (g) a fraction 43 of initial boiling point below 350‹ C. and final boiling point between 450‹ and 550‹ C. Suitable feeds 1 are residues from the atmospheric or vacuum distillation of crude oil, heavy crude oil, thermal cracking residues, oxygen-treated residual oil, or tar. The hydrocracking step (1) is carried out at 250-500‹ C. and 35-500 kg/ cm.<SP>2</SP> abs. using a fixed bed of one or more of Mo, W, Cr, Ni, Co and Fe or their oxides or sulphides supported on alumina which can contain F and P, magnesia, zirconia, titania or boria. The hydrotreating of fraction (a) is carried out at 5-70 kg/cm.<SP>2</SP> and 275-400‹ C. using a catalyst containing Cr, Mo, W, Fe, Co and/or Ni to promote hydrodesulphurization or of Pt, Pd, Rh, Ru, Os or Ir on alumina or silica to promote the hydrogenation of aromatics. The hydrocracking of fraction (b) is carried out at 70-200 kg/cm.<SP>2</SP> and 275-450‹ C., using a catalyst containing one or more of Ag, An, Cu, Mo, W, Cr, Fe, Ni, Co, Pt, Pd, Rh, Ru, Ir or Os on silica, alumina, zirconia, titania and/or boria and which can contain F. The separation (5) provides a stream 39 containing liquid petroleum gases and gasoline boiling up to 100‹ C.; a stream 40 of naphtha fraction (d) which can be catalytically reformed to convert naphthenes to aromatics and used as a motor gasoline component; a stream 41 of kerosine fraction (e); a stream 42 of diesel fuel (f); and a stream 43 of fraction (g). The kerosine fraction 42 can be used as a jet fuel after being hydrogenated at 47 to saturate aromatics at 100-350‹ C. and 20-100 kg/cm.<SP>2</SP>, using a catalyst of Ni on diatomaceous earth or of Rh or Pt on alumina containing 0À1- 10 wt. per cent F or Cl; the effluent from the reactor 47 is separated at 52 into a hydrogenated kerosine 54 and a lighter fraction 53. The fraction 43 can be used for the production of lube oil, as a catalytic cracking feed or recycled to the hydrocracking unit 32.
GB5169969A 1969-10-22 1969-10-22 Process for the convesion of a hydrocarbon oil containing residual material Expired GB1221275A (en)

Priority Applications (6)

Application Number Priority Date Filing Date Title
GB5169969A GB1221275A (en) 1969-10-22 1969-10-22 Process for the convesion of a hydrocarbon oil containing residual material
NL7006961A NL166495C (en) 1969-10-22 1970-05-14 METHOD FOR CONVERTING A HYDROCARBON OIL CONTAINING RESIDUAL MATERIAL
JP9172270A JPS511726B1 (en) 1969-10-22 1970-10-20
FR7037830A FR2065459B1 (en) 1969-10-22 1970-10-20
DE19702051475 DE2051475C2 (en) 1969-10-22 1970-10-20 Process for converting a hydrocarbon oil containing a residue by hydrocracking and hydrofining
CA096063A CA927766A (en) 1969-10-22 1970-10-20 Process for the conversion of a hydrocarbon oil containing residual material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB5169969A GB1221275A (en) 1969-10-22 1969-10-22 Process for the convesion of a hydrocarbon oil containing residual material

Publications (1)

Publication Number Publication Date
GB1221275A true GB1221275A (en) 1971-02-03

Family

ID=10461033

Family Applications (1)

Application Number Title Priority Date Filing Date
GB5169969A Expired GB1221275A (en) 1969-10-22 1969-10-22 Process for the convesion of a hydrocarbon oil containing residual material

Country Status (6)

Country Link
JP (1) JPS511726B1 (en)
CA (1) CA927766A (en)
DE (1) DE2051475C2 (en)
FR (1) FR2065459B1 (en)
GB (1) GB1221275A (en)
NL (1) NL166495C (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0271148A1 (en) * 1986-12-10 1988-06-15 Shell Internationale Researchmaatschappij B.V. Process for the manufacture of kerosine and/or gas oils
WO2010074756A2 (en) 2008-12-24 2010-07-01 Exxonmobil Research And Engineering Company Co-processing of diesel biofeed and heavy oil
WO2017101985A1 (en) * 2015-12-15 2017-06-22 Sabic Global Technologies B.V. Process for producing c2 and c3 hydrocarbons
WO2018060938A1 (en) * 2016-09-30 2018-04-05 Hindustan Petroleum Corporation Limited A process for upgrading heavy hydrocarbons
EP3567090A1 (en) * 2018-05-11 2019-11-13 Inner Mongolia Shengyuan Technology Co., Ltd. Combined hydrogenation process method for producing high-quality fuel by medium-low-temperature coal tar

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
NL7001246A (en) * 1970-01-29 1971-08-02
CN109503183B (en) * 2018-12-26 2022-03-18 武汉钢铁集团耐火材料有限责任公司 Converter large-surface repairing material and preparation method thereof

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3132087A (en) * 1961-08-30 1964-05-05 Union Oil Co Manufacture of gasoline and jet fuel by hydrocracking

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0271148A1 (en) * 1986-12-10 1988-06-15 Shell Internationale Researchmaatschappij B.V. Process for the manufacture of kerosine and/or gas oils
WO2010074756A2 (en) 2008-12-24 2010-07-01 Exxonmobil Research And Engineering Company Co-processing of diesel biofeed and heavy oil
WO2010074756A3 (en) * 2008-12-24 2011-05-26 Exxonmobil Research And Engineering Company Co-processing of diesel biofeed and heavy oil
US8632675B2 (en) 2008-12-24 2014-01-21 Exxonmobil Research And Engineering Company Co-processing of diesel biofeed and heavy oil
US10526551B2 (en) 2014-12-22 2020-01-07 Sabic Global Technologies B.V. Process for producing C2 and C3 hydrocarbons
WO2017101985A1 (en) * 2015-12-15 2017-06-22 Sabic Global Technologies B.V. Process for producing c2 and c3 hydrocarbons
WO2018060938A1 (en) * 2016-09-30 2018-04-05 Hindustan Petroleum Corporation Limited A process for upgrading heavy hydrocarbons
US10988697B2 (en) 2016-09-30 2021-04-27 Hindustan Petroleum Corporation Limited Process for upgrading heavy hydrocarbons
EP3567090A1 (en) * 2018-05-11 2019-11-13 Inner Mongolia Shengyuan Technology Co., Ltd. Combined hydrogenation process method for producing high-quality fuel by medium-low-temperature coal tar

Also Published As

Publication number Publication date
JPS511726B1 (en) 1976-01-20
FR2065459B1 (en) 1973-10-19
NL166495B (en) 1981-03-16
CA927766A (en) 1973-06-05
NL166495C (en) 1981-08-17
FR2065459A1 (en) 1971-07-30
DE2051475C2 (en) 1982-12-09
NL7006961A (en) 1970-08-25
DE2051475A1 (en) 1971-04-29

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