GB1504586A - Process for the catalytic hydrodesulphurisation of vanadium- and nickelcontaining residual hydrocarbon oils - Google Patents
Process for the catalytic hydrodesulphurisation of vanadium- and nickelcontaining residual hydrocarbon oilsInfo
- Publication number
- GB1504586A GB1504586A GB10508/75A GB1050875A GB1504586A GB 1504586 A GB1504586 A GB 1504586A GB 10508/75 A GB10508/75 A GB 10508/75A GB 1050875 A GB1050875 A GB 1050875A GB 1504586 A GB1504586 A GB 1504586A
- Authority
- GB
- United Kingdom
- Prior art keywords
- catalyst
- catalysts
- combination
- weight
- requirement
- 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
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
-
- 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
1504586 Hydrodesulphurization of heavy oils SHELL INTERNATIONALE RESEARCH MAATSCHAPPIJ BV 13 March 1975 [11 April 1974] 10508/75 Heading C5E In a process for the catalytic hydrodesulphurization of vanadium- and nickel-containing residual hydrocarbon oils without catalyst replenishment, the hydrocarbon oil is consecutively contacted with a catalyst I and a catalyst II which satisfy the requirements: (a) each of the individual catalysts of which the combination of catalyst I and catalyst II is composed has a total pore volume in excess of 0À30 ml./g. of which less than 10% is present as pores having a diameter in excess of 100 nm., (b) catalyst II has a specific average pore diameter (p) and a specific average particle diameter (d) such that the quotient p/(d)<SP>0À9</SP> of catalyst II satisfies the requirement where P H2 is the hydrogen partial pressure applied, (c) when the combination of catalyst I and catalyst II is composed of two catalysts, catalyst I has a p and d such that the quotient p/(d)<SP>0.9</SP> of catalyst I satisfies the requirement while when the combination of catalyst I and catalyst II is composed of more than two catalysts, the above requirement in respect of [p/(d)<SP>0À9</SP>]cat.I applies to the average p/(d)<SP>0À9</SP> of catalyst I determined as the weight average of the values of p/(d)<SP>0À9</SP> of each of the individual catalysts of which catalyst I is composed, (d) the percentage of the total catalyst volume which is taken up by catalyst II is between 10 and 90% and satisfies the requirement: Sf representing the sulphur content of the feed and Sp the sulphur content of the desulphurized product, and (e) when the combination of catalyst I and catalyst II is composed of more than two catalysts, each of the individual catalysts of which catalyst I is composed has a p and d such that the quotient p/(d)<SP>0À9</SP> of each of these catalysts is greater than [p/(d)<SP>0À9</SP>]cat.II, p being in nm., d in mm., P H2 in bar and Sp and Sf in weight per cent. The designation catalyst II is defined as being the second catalyst when a combination of two catalysts is used and as being the final catalyst when using a combination of more than two catalysts, the designation catalyst I being defined as being the first catalyst when two catalysts are used and all but the last catalyst when more than two are used. The catalysts used preferably contain 0À5 to 20 parts by weight of nickel and/or cobalt and 2À5 to 60 parts by weight of molybdenum and/or tungsten per 100 parts by weight of carrier, the metals being present on the carrier in metallic form or in the form of their oxides or sulphides, suitable carriers being the oxides of elements of Groups II, III and IV of the periodic system, e.g. silica, alumina, magnesia, zirconia and mixtures thereof.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
NLAANVRAGE7404948,A NL187641C (en) | 1974-04-11 | 1974-04-11 | PROCESS FOR CATALYTIC HYDROGENIZING DESULFULIFYING WITHOUT CATALYST REPLACEMENT OF RESIDUAL HYDROCARBON OILS. |
Publications (1)
Publication Number | Publication Date |
---|---|
GB1504586A true GB1504586A (en) | 1978-03-22 |
Family
ID=19821155
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB10508/75A Expired GB1504586A (en) | 1974-04-11 | 1975-03-13 | Process for the catalytic hydrodesulphurisation of vanadium- and nickelcontaining residual hydrocarbon oils |
Country Status (13)
Country | Link |
---|---|
JP (1) | JPS6027714B2 (en) |
BE (1) | BE827492A (en) |
CA (1) | CA1060370A (en) |
DE (1) | DE2512294A1 (en) |
DK (1) | DK129375A (en) |
ES (1) | ES435948A1 (en) |
FR (1) | FR2267359B1 (en) |
GB (1) | GB1504586A (en) |
IT (1) | IT1034407B (en) |
NL (1) | NL187641C (en) |
NO (1) | NO144424C (en) |
SE (1) | SE408431B (en) |
ZA (1) | ZA751655B (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5492684A (en) * | 1993-07-06 | 1996-02-20 | Mobil Oil Corporation | Graded-bed system for improved separations |
US6280610B1 (en) | 1995-06-08 | 2001-08-28 | Akzo Nobel Nv | Hydrotreating catalyst: composition, preparation, and use thereof |
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 (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6215231U (en) * | 1985-07-11 | 1987-01-29 | ||
JPH0311812U (en) * | 1989-06-21 | 1991-02-06 |
-
1974
- 1974-04-11 NL NLAANVRAGE7404948,A patent/NL187641C/en not_active IP Right Cessation
-
1975
- 1975-02-24 CA CA220,643A patent/CA1060370A/en not_active Expired
- 1975-03-13 NO NO750853A patent/NO144424C/en unknown
- 1975-03-13 GB GB10508/75A patent/GB1504586A/en not_active Expired
- 1975-03-14 SE SE7502921A patent/SE408431B/en not_active IP Right Cessation
- 1975-03-18 IT IT21422/75A patent/IT1034407B/en active
- 1975-03-18 ZA ZA00751655A patent/ZA751655B/en unknown
- 1975-03-20 DE DE19752512294 patent/DE2512294A1/en active Granted
- 1975-03-24 ES ES435948A patent/ES435948A1/en not_active Expired
- 1975-03-26 DK DK129375A patent/DK129375A/da not_active IP Right Cessation
- 1975-03-26 FR FR7509481A patent/FR2267359B1/fr not_active Expired
- 1975-04-02 JP JP50039308A patent/JPS6027714B2/en not_active Expired
- 1975-04-03 BE BE1006570A patent/BE827492A/en unknown
Cited By (14)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5492684A (en) * | 1993-07-06 | 1996-02-20 | Mobil Oil Corporation | Graded-bed system for improved separations |
US6280610B1 (en) | 1995-06-08 | 2001-08-28 | Akzo Nobel Nv | Hydrotreating catalyst: composition, preparation, and use thereof |
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 |
---|---|
NO144424C (en) | 1981-08-26 |
AU7921175A (en) | 1976-09-23 |
NL7404948A (en) | 1975-10-14 |
JPS50136302A (en) | 1975-10-29 |
FR2267359B1 (en) | 1982-03-19 |
SE408431B (en) | 1979-06-11 |
ZA751655B (en) | 1976-02-25 |
DK129375A (en) | 1975-10-12 |
FR2267359A1 (en) | 1975-11-07 |
ES435948A1 (en) | 1976-12-16 |
DE2512294C2 (en) | 1987-08-27 |
NL187641B (en) | 1991-07-01 |
DE2512294A1 (en) | 1975-10-23 |
NL187641C (en) | 1991-12-02 |
BE827492A (en) | 1975-10-03 |
SE7502921L (en) | 1975-10-12 |
CA1060370A (en) | 1979-08-14 |
NO750853L (en) | 1975-10-14 |
JPS6027714B2 (en) | 1985-07-01 |
NO144424B (en) | 1981-05-18 |
IT1034407B (en) | 1979-09-10 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US3114701A (en) | Catalytic hydrodenitrification process | |
US2687370A (en) | Conversion of hydrocarbons with nickel oxide-molybdenum oxide catalyst | |
CA2045447C (en) | Aromatics saturation process for diesel boiling-range hydrocarbons | |
EP0127220B1 (en) | Catalyst preparation | |
GB1510155A (en) | Hydrocarbon conversion catalyst comprising alumina and aluminum phosphate | |
EP0167215B1 (en) | Process for the preparation of hydrocarbons | |
ES442289A1 (en) | Hydrocarbon conversion with an acidic multimetallic catalytic composite | |
CA1171882A (en) | Process and catalyst for the preparation of a gas mixture having a high content of c.sub.2- hydrocarbons | |
GB1356400A (en) | Method of reforming hydrocarbons and catalyst therefor | |
GB1354968A (en) | Process for the preparation of a hydrogenation catalyst | |
GB1504586A (en) | Process for the catalytic hydrodesulphurisation of vanadium- and nickelcontaining residual hydrocarbon oils | |
US2574448A (en) | Catalytic desulfurization of gas oil | |
GB1504951A (en) | Hydrogenation of unsaturated hydrocarbons | |
GB2161716A (en) | Cobalt-containing catalyst activation | |
US3530194A (en) | Process for the catalytic conversion of hydrocarbons with steam | |
US3425934A (en) | Catalytic refining with hydrogen | |
US3016346A (en) | Hydrodesulfurization process and catalyst therefor | |
GB1505886A (en) | Process for the catalytic hydrodesulphurisation of vanadium-and nickel-containing residual hydrocarbon oils | |
GB1496959A (en) | Hydrocarbon conversion process and catalytic composite for use therein | |
GB1522629A (en) | Process for the preparation of catalysts | |
US2574447A (en) | Catalytic desulfurization of petroleum hydrocarbons | |
CA1102778A (en) | Hydroconversion catalyst and process | |
US3691063A (en) | Residual fuel oil hydrocracking process | |
US2706209A (en) | Purification of crude benzene | |
US2574450A (en) | Desulfurization of hydrocarbon extracts |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PS | Patent sealed [section 19, patents act 1949] | ||
PCNP | Patent ceased through non-payment of renewal fee |
Effective date: 19930313 |