GB1264373A - - Google Patents
Info
- Publication number
- GB1264373A GB1264373A GB1264373DA GB1264373A GB 1264373 A GB1264373 A GB 1264373A GB 1264373D A GB1264373D A GB 1264373DA GB 1264373 A GB1264373 A GB 1264373A
- Authority
- GB
- United Kingdom
- Prior art keywords
- stream
- compounds
- separated
- boiling
- hydro
- 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
- C10G65/00—Treatment of hydrocarbon oils by two or more hydrotreatment processes only
Abstract
1,264,373. Hydrofining; recovering aromatic hydrocarbons. BETHLEHEM STEEL CORP. 5 June, 1969 [6 June, 1968], No. 28568/69. Heading C5E. A crude aromatic oil stream 11 boiling at up to 200 C., e.g. resulting from the carbonization of coal, and containing polymerizable compounds, non-aromatic compounds, oxygen compounds and sulphur compounds is separated into a stream 13 boiling below 120 C. and a stream 31 boiling above 120 C. Components boiling below 80 C. are removed from the stream 13 at 14 and the stream is then vaporized by mixing with the stream 17 of hot recycle hydrogen. The vapour stream 19 produced is reacted in the reactors 21, 22 and 23 at 550- 675 C. and 28-105 kg./cm.<SP>2</SP> gauge using a chromia-alumina catalyst to hydrocrack olefins, paraffins and naphthalene to C 1 to C 4 hydrocarbons, to hydrogenate sulphur compounds and to hydrodealkylate toluene. The stream 31 is distilled at 32 to remove a stream 37 from which naphthalene can be recovered and the 120- 200 C. fraction 33 is vaporized by mixing with the hot recycle hydrogen stream 38. The vaporized stream is reacted in the pretreater 34 at 250-375 C. and 21-105 kg. cm.<SP>2</SP> gauge using a catalyst of sulphided nickel molybdate or copper molybdate on alumina to convert polymerizable components to non-polymerizable components and oxygen-containing compounds to hydrocarbons and water. The effluent from the pretreater 34 is condensed and the stream 45, after separation at 43 of the gas 47 and the water 44 is passed to the second stage 22 of the hydro-upgrading zone. The gaseous effluent 24 from the reactor 23 is condensed and separated at 27 into a gaseous stream 28 and a liquid stream 29 which is separated into a H 2 S- and C 1 -C 4 hydrocarbon-containing stream 62, and after treatment with clay at 64 is separated into a pure benzene stream 70, a toluene stream 71 which is recycled to the hydro-upgrading zone 21, 22, 23 in admixture with the low boiling stream 16, a C 8 stream 72 comprising xylenes and ethyl benzene, a C 9 stream 73 which is recycled to the zone 23 with the pretreated stream 45 and a C 10 - and biphenyl-containing stream 74 which is recycled to the second hydro-upgrading zone 22.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US73513168A | 1968-06-06 | 1968-06-06 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB1264373A true GB1264373A (en) | 1972-02-23 |
Family
ID=24954502
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB1264373D Expired GB1264373A (en) | 1968-06-06 | 1969-06-05 |
Country Status (4)
Country | Link |
---|---|
US (1) | US3449460A (en) |
CA (1) | CA927846A (en) |
DE (1) | DE1928386A1 (en) |
GB (1) | GB1264373A (en) |
Families Citing this family (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3717570A (en) * | 1971-02-05 | 1973-02-20 | J Hochman | Simultaneous hydrofining of coker gas oil, vacuum gas oils and virgin kerosene |
EP0582723A1 (en) * | 1992-08-04 | 1994-02-16 | NEUMANN + STALLHERM GmbH | Process for upgrading crude benzene |
EP0708167B1 (en) * | 1994-10-22 | 1997-12-03 | Krupp Uhde GmbH | Process for the production of a precursor product containing aromatic hydrocarbons for the recuperation of aromatics from raw coking benzene |
CN100457861C (en) * | 2006-01-19 | 2009-02-04 | 中国石油化工股份有限公司 | Method for producing high grade of diesel oil by charking full distillate oil |
CN100448957C (en) * | 2006-01-19 | 2009-01-07 | 中国石油化工股份有限公司 | Process method for charking full distillate oil |
CN105473690B (en) * | 2013-07-02 | 2018-01-09 | 沙特基础工业公司 | For by converting crude oil into the method and facility of the petrochemical industry product with improved carbon efficiencies |
Family Cites Families (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3081259A (en) * | 1963-03-12 | Coke oven light oil purification | ||
US3094481A (en) * | 1960-09-09 | 1963-06-18 | Exxon Research Engineering Co | Hydrofining process with temperature control |
US3207802A (en) * | 1960-12-14 | 1965-09-21 | Air Prod & Chem | Purification of coke-oven light oil |
US3267021A (en) * | 1964-03-30 | 1966-08-16 | Chevron Res | Multi-stage hydrocracking process |
US3260765A (en) * | 1965-05-25 | 1966-07-12 | Universal Oil Prod Co | Treatment of alkyl-substituted aromatic compounds |
-
1968
- 1968-06-06 US US735131A patent/US3449460A/en not_active Expired - Lifetime
-
1969
- 1969-06-04 DE DE19691928386 patent/DE1928386A1/en active Pending
- 1969-06-05 CA CA053537A patent/CA927846A/en not_active Expired
- 1969-06-05 GB GB1264373D patent/GB1264373A/en not_active Expired
Also Published As
Publication number | Publication date |
---|---|
DE1928386A1 (en) | 1969-12-11 |
US3449460A (en) | 1969-06-10 |
CA927846A (en) | 1973-06-05 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
PS | Patent sealed [section 19, patents act 1949] | ||
PCNP | Patent ceased through non-payment of renewal fee |