GB1335348A - Desulphurisation of hydrocarbon oils - Google Patents
Desulphurisation of hydrocarbon oilsInfo
- Publication number
- GB1335348A GB1335348A GB1335348DA GB1335348A GB 1335348 A GB1335348 A GB 1335348A GB 1335348D A GB1335348D A GB 1335348DA GB 1335348 A GB1335348 A GB 1335348A
- Authority
- GB
- United Kingdom
- Prior art keywords
- gas
- passed
- fraction
- column
- lighter fraction
- 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
- C10G49/00—Treatment 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
- C10G49/007—Treatment 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
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
- C01B3/02—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
- C01B3/32—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air
- C01B3/34—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents
- C01B3/38—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents using catalysts
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Health & Medical Sciences (AREA)
- General Health & Medical Sciences (AREA)
- Combustion & Propulsion (AREA)
- Inorganic Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
1335348 Desulphurized fuel gases WHESSOE Ltd 19 April 1971 [19 Feb 1970] 7942/70 Heading C5E Hydrocarbon oils are separated into a heavier fraction and a lighter fraction and the heavier fraction is hydrogenated using a hydrogenation gas provided by processing at least a portion of the lighter fraction. A crude oil 1 is distilled at 4 to provide a heavier fraction 5 and a lighter fraction 8. The heavier fraction is hydrogenated in a fluid bed 7 with a hydrogenating gas 12 to produce a product gas which is quenched at 13 with a water spray to 250-300‹ C., further cooled at 15 and separated at 16 into a condensate 17 containing benzene, toluene and xylene, a portion of which can be recycled to the hydrogenator 7 to upgrade the benzene, toluene and xylene, and a gas 16. The gas 16 is passed to an absorber 18 to remove sulphur and produce a desulphurized fuel gas. The sulphur rich absorbent is passed to a tower 19 in which its pressure is reduced and the hydrogen sulphide 22 liberated is converted to liquid sulphur 24 and the regenerated absorbent is returned to the column 18. The lighter fraction 8 is condensed at 26, in part returned to the column 4 and in part passed through desulphurizer vessels 32, 33 and 34. The desulphurized effluent from 34 is reacted with steam 37 in the catalytic reformer 35 which is heated by off-gas from the column 4. The effluent from the reformer 35 is cooled and passed to a shift converter 40. After cooling and passage through a carbon dioxide absorption column 43 the hydrogenation gas is compressed, preheated and passed into the hydrogenator 7. Suitably 20-40% of the crude oil is separated as the lighter fraction 8. A portion of the fuel gas product can be recycled to the reformer 35.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB794270 | 1971-04-19 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB1335348A true GB1335348A (en) | 1973-10-24 |
Family
ID=9842741
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB1335348D Expired GB1335348A (en) | 1971-04-19 | 1971-04-19 | Desulphurisation of hydrocarbon oils |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB1335348A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US8372267B2 (en) | 2008-07-14 | 2013-02-12 | Saudi Arabian Oil Company | Process for the sequential hydroconversion and hydrodesulfurization of whole crude oil |
US8491779B2 (en) | 2009-06-22 | 2013-07-23 | Saudi Arabian Oil Company | Alternative process for treatment of heavy crudes in a coking refinery |
US8632673B2 (en) | 2007-11-28 | 2014-01-21 | Saudi Arabian Oil Company | Process for catalytic hydrotreating of sour crude oils |
US9260671B2 (en) | 2008-07-14 | 2016-02-16 | Saudi Arabian Oil Company | Process for the treatment of heavy oils using light hydrocarbon components as a diluent |
-
1971
- 1971-04-19 GB GB1335348D patent/GB1335348A/en not_active Expired
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US8632673B2 (en) | 2007-11-28 | 2014-01-21 | Saudi Arabian Oil Company | Process for catalytic hydrotreating of sour crude oils |
US8372267B2 (en) | 2008-07-14 | 2013-02-12 | Saudi Arabian Oil Company | Process for the sequential hydroconversion and hydrodesulfurization of whole crude oil |
US9260671B2 (en) | 2008-07-14 | 2016-02-16 | Saudi Arabian Oil Company | Process for the treatment of heavy oils using light hydrocarbon components as a diluent |
US8491779B2 (en) | 2009-06-22 | 2013-07-23 | Saudi Arabian Oil Company | Alternative process for treatment of heavy crudes in a coking refinery |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
PS | Patent sealed | ||
PLNP | Patent lapsed through nonpayment of renewal fees |