GB1324167A - Process for the catalytic hydroconversion of a residual hydrocarbon oil - Google Patents

Process for the catalytic hydroconversion of a residual hydrocarbon oil

Info

Publication number
GB1324167A
GB1324167A GB5635769A GB1324167DA GB1324167A GB 1324167 A GB1324167 A GB 1324167A GB 5635769 A GB5635769 A GB 5635769A GB 1324167D A GB1324167D A GB 1324167DA GB 1324167 A GB1324167 A GB 1324167A
Authority
GB
United Kingdom
Prior art keywords
oil
hydrogen sulphide
residual hydrocarbon
beginning
precursor
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
GB5635769A
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
Publication of GB1324167A publication Critical patent/GB1324167A/en
Expired legal-status Critical Current

Links

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
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
    • B01J8/0207—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid flow within the bed being predominantly horizontal
    • B01J8/0214—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid flow within the bed being predominantly horizontal in a cylindrical annular shaped bed
    • 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

1324167 Hydrotreating residual hydrocarbon oils SHELL INTERNATIONALE RESEARCH MAATSCHAPPIJ NV 6 Oct 1970 [18 Nov 1969] 56357/69 Heading C5E In the catalytic hydroconversion of residual hydrocarbon oils, e.g. to remove sulphur, substantially in the liquid phase hydrogen sulphide and/or hydrogen sulphide precursor is added to the oil in an amount which corresponds to at least 0À5% wt. hydrogen sulphide, calculated on fresh oil, at the beginning of the process and which is decreased continuously or stepwise in the course of the process to less than 80% of the amount added at the beginning. The hydrogen sulphide or precursor can be provided by adding hydrogen sulphide, sulphur dioxide, alkyl mercaptan or carbon disulphide to the oil or to the hydrogen or by recycling a portion of the product oil which has not been depressurized. The residual oil treated can be a topped crude oil or a long or short residue and can be pretreated by flashing, deasphalting or non-catalytic hydrorefining; visbreaker effluent or tar sand oil can be used. The catalyst used, suitably comprising cobalt and molybdenum on alumina, can be presulphided and can be used in a radial flow bed or in an axial flow bed with upflow or downflow of the oil. The hydrodesulphurization is carried out at 300-475‹ C. and 30-350 kg./cm<SP>2</SP>.
GB5635769A 1969-11-18 1969-11-18 Process for the catalytic hydroconversion of a residual hydrocarbon oil Expired GB1324167A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB5635769 1969-11-18

Publications (1)

Publication Number Publication Date
GB1324167A true GB1324167A (en) 1973-07-18

Family

ID=10476421

Family Applications (1)

Application Number Title Priority Date Filing Date
GB5635769A Expired GB1324167A (en) 1969-11-18 1969-11-18 Process for the catalytic hydroconversion of a residual hydrocarbon oil

Country Status (9)

Country Link
US (1) US3714031A (en)
JP (1) JPS5030644B1 (en)
BE (1) BE758565A (en)
CA (1) CA926333A (en)
DE (1) DE2054771A1 (en)
FR (1) FR2067349B1 (en)
GB (1) GB1324167A (en)
NL (1) NL7016190A (en)
ZA (1) ZA706922B (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0183364A1 (en) * 1984-11-30 1986-06-04 Mobil Oil Corporation Process for producing stabilizing hydroprocessed lubricating oil stocks by the addition of hydrogen sulfide
US11136513B2 (en) 2017-02-12 2021-10-05 Magëmä Technology LLC Multi-stage device and process for production of a low sulfur heavy marine fuel oil from distressed heavy fuel oil materials
US11203722B2 (en) 2017-02-12 2021-12-21 Magëmä Technology LLC Multi-stage process and device for treatment heavy marine fuel oil and resultant composition including ultrasound promoted desulfurization
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

Families Citing this family (25)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4547285A (en) * 1983-10-24 1985-10-15 Union Oil Company Of California Hydrotreating process wherein sulfur is added to the feedstock to maintain the catalyst in sulfided form
US4980046A (en) * 1989-12-28 1990-12-25 Uop Separation system for hydrotreater effluent having reduced hydrocarbon loss
US5275994A (en) * 1991-06-17 1994-01-04 Texaco Inc. Process for preparing a catalyst for removal of hydroprocessing impurities
CA2393753C (en) * 1999-12-22 2010-07-20 Bruce Randall Cook High temperature depressurization for naphtha mercaptan removal
US6387249B1 (en) * 1999-12-22 2002-05-14 Exxonmobil Research And Engineering Company High temperature depressurization for naphtha mercaptan removal
US7444305B2 (en) * 2001-02-15 2008-10-28 Mass Connections, Inc. Methods of coordinating products and service demonstrations
US20070000808A1 (en) * 2003-12-19 2007-01-04 Bhan Opinder K Method and catalyst for producing a crude product having selected properties
US20060289340A1 (en) * 2003-12-19 2006-12-28 Brownscombe Thomas F Methods for producing a total product in the presence of sulfur
US7628908B2 (en) * 2003-12-19 2009-12-08 Shell Oil Company Systems, methods, and catalysts for producing a crude product
US7879223B2 (en) * 2003-12-19 2011-02-01 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
US7745369B2 (en) * 2003-12-19 2010-06-29 Shell Oil Company Method and catalyst for producing a crude product with minimal hydrogen uptake
US20070000810A1 (en) * 2003-12-19 2007-01-04 Bhan Opinder K Method for producing a crude product with reduced tan
TW200602591A (en) * 2004-07-08 2006-01-16 hong-yang Chen Gas supply device by gasifying burnable liquid
TWI415930B (en) * 2005-04-06 2013-11-21 Shell Int Research A process for reducing the total acid number (tan) of a liquid hydrocarbonaceous feedstock
CA2604015C (en) * 2005-04-11 2014-02-18 Shell International Research Maatschappij B.V. Systems, methods, and catalysts for producing a crude product
EP1874897A1 (en) 2005-04-11 2008-01-09 Shell Internationale Research Maatschappij B.V. Method and catalyst for producing a crude product having a reduced mcr content
BRPI0609416A2 (en) * 2005-04-11 2011-10-11 Shell Int Research method to produce a gross product
EP1869144A1 (en) * 2005-04-11 2007-12-26 Shell International Research Maatschappij B.V. Method and catalyst for producing a crude product having a reduced nitrogen content
WO2007149917A1 (en) * 2006-06-22 2007-12-27 Shell Oil Company Methods for producing a total product with selective hydrocarbon production
WO2007149921A1 (en) * 2006-06-22 2007-12-27 Shell Oil Company Methods for producing a crude product from selected feed
US20070295646A1 (en) * 2006-06-22 2007-12-27 Bhan Opinder K Method for producing a crude product with a long-life catalyst
US20080087578A1 (en) * 2006-10-06 2008-04-17 Bhan Opinder K Methods for producing a crude product and compositions thereof
US8945372B2 (en) 2011-09-15 2015-02-03 E I Du Pont De Nemours And Company Two phase hydroprocessing process as pretreatment for tree-phase hydroprocessing process
CN106378063B (en) * 2015-08-04 2018-11-16 中国石化工程建设有限公司 A kind of methanator and methanation process

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3441500A (en) * 1966-08-04 1969-04-29 Sinclair Research Inc Process for activating a fixed bed of hydrorefining catalyst

Cited By (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0183364A1 (en) * 1984-11-30 1986-06-04 Mobil Oil Corporation Process for producing stabilizing hydroprocessed lubricating oil stocks by the addition of hydrogen sulfide
US11136513B2 (en) 2017-02-12 2021-10-05 Magëmä Technology LLC Multi-stage device and process for production of a low sulfur heavy marine fuel oil from distressed heavy fuel oil materials
US11203722B2 (en) 2017-02-12 2021-12-21 Magëmä Technology LLC Multi-stage process and device for treatment heavy marine fuel oil and resultant composition including ultrasound promoted desulfurization
US11345863B2 (en) 2017-02-12 2022-05-31 Magema Technology, Llc Heavy marine fuel oil composition
US11441084B2 (en) 2017-02-12 2022-09-13 Magēmā Technology LLC Multi-stage device and process for production of a low sulfur heavy marine fuel oil
US11447706B2 (en) 2017-02-12 2022-09-20 Magēmā Technology LLC Heavy marine fuel compositions
US11492559B2 (en) 2017-02-12 2022-11-08 Magema Technology, Llc Process and device for reducing environmental contaminates in heavy marine fuel oil
US11530360B2 (en) 2017-02-12 2022-12-20 Magēmā Technology LLC Process and device for treating high sulfur heavy marine fuel oil for use as feedstock in a subsequent refinery unit
US11560520B2 (en) 2017-02-12 2023-01-24 Magēmā Technology LLC Multi-stage process and device for treatment heavy marine fuel oil 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
US11795406B2 (en) 2017-02-12 2023-10-24 Magemä Technology LLC Multi-stage device and process for production of a low sulfur heavy marine fuel oil from distressed heavy fuel oil materials
US11884883B2 (en) 2017-02-12 2024-01-30 MagêmãTechnology LLC Multi-stage device and process for production of a low sulfur heavy marine fuel oil
US11912945B2 (en) 2017-02-12 2024-02-27 Magēmā Technology LLC Process and device for treating high sulfur heavy marine fuel oil for use as feedstock in a subsequent refinery unit

Also Published As

Publication number Publication date
US3714031A (en) 1973-01-30
ZA706922B (en) 1971-07-28
FR2067349B1 (en) 1973-11-23
JPS5030644B1 (en) 1975-10-02
NL7016190A (en) 1971-05-21
CA926333A (en) 1973-05-15
FR2067349A1 (en) 1971-08-20
DE2054771A1 (en) 1971-05-27
BE758565A (en) 1971-05-06

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Legal Events

Date Code Title Description
PS Patent sealed [section 19, patents act 1949]
PLNP Patent lapsed through nonpayment of renewal fees