GB904993A - Process for the separation of naphthalene and its derivatives from benzene and its derivatives - Google Patents
Process for the separation of naphthalene and its derivatives from benzene and its derivativesInfo
- Publication number
- GB904993A GB904993A GB1067961A GB1067961A GB904993A GB 904993 A GB904993 A GB 904993A GB 1067961 A GB1067961 A GB 1067961A GB 1067961 A GB1067961 A GB 1067961A GB 904993 A GB904993 A GB 904993A
- Authority
- GB
- United Kingdom
- Prior art keywords
- feed
- sulpholane
- naphthalenes
- boiling
- extract
- 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
- C10G21/00—Refining of hydrocarbon oils, in the absence of hydrogen, by extraction with selective solvents
Landscapes
- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
Naphthalenes of differing carbon number are separated from alkyl benzenes of comparable carbon number by liquid-liquid extraction with a sulpholane type solvent to obtain an extract enriched in naphthalenes and a raffinate enriched in benzenes. The difference in carbon number between the highest and lowest hydrocarbons in the feed is preferably from 5-8; suitable feeds are obtained from coker gas oil and cycle gas oil from a catalytic cracking. The sulpholane solvent may contain alkyl substituents or polar groups containing oxygen, nitrogen, sulphur or halogen, e.g. those described in Specification 625,505. The specific gravity of the sulpholane is preferably at least 0.2 above or below that of the feed and is used in a weight ratio to feed of 0.2-2.0. In a preferred embodiment a feed e.g. boiling from 160-315 DEG C. also containing saturated hydrocarbons is distilled to obtain a fraction boiling below the naphthalene-containing feed, e.g. 160-205 DEG C., having a higher saturate content than the total feed, and a side stream, e.g. boiling from 195-235 DEG C. which is subjected to extraction, and the lower boiling fraction is used as a countersolvent in the extraction, being introduced at the end where the extract is removed. The naphthalenes are preferably recovered from the extract by a further extraction with a non-polar solvent immiscible with the sulpholane and boiling below the naphthalenes, e.g. a C1-10 paraffin, which is used in a weight ratio to extract of 0.2-2.0 and separated from the naphthalene by distillation.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DES73177A DE1149478B (en) | 1961-03-27 | 1961-03-27 | Process for the separation of condensed diaromatic from monoaromatic hydrocarbons by means of a selective solvent |
Publications (1)
Publication Number | Publication Date |
---|---|
GB904993A true GB904993A (en) | 1962-09-05 |
Family
ID=7503717
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB1067961A Expired GB904993A (en) | 1961-03-27 | 1961-03-23 | Process for the separation of naphthalene and its derivatives from benzene and its derivatives |
Country Status (2)
Country | Link |
---|---|
DE (1) | DE1149478B (en) |
GB (1) | GB904993A (en) |
Family Cites Families (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
NL64177C (en) * | 1943-02-08 | |||
DE865171C (en) * | 1948-06-08 | 1953-01-29 | Anglo Iranian Oil Co Ltd | Process for the selective extraction and extractive distillation of hydrocarbon mixtures |
FR991592A (en) * | 1949-08-03 | 1951-10-08 | Anglo Iranian Oil Co Ltd | Process for the separation of organic compounds, in particular hydrocarbons |
US2831039A (en) * | 1955-04-04 | 1958-04-15 | Standard Oil Co | Solvent extraction |
-
1961
- 1961-03-23 GB GB1067961A patent/GB904993A/en not_active Expired
- 1961-03-27 DE DES73177A patent/DE1149478B/en active Pending
Also Published As
Publication number | Publication date |
---|---|
DE1149478B (en) | 1963-05-30 |
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