GB786305A - A process for isomerizing dialkyl benzenes in the liquid phase - Google Patents
A process for isomerizing dialkyl benzenes in the liquid phaseInfo
- Publication number
- GB786305A GB786305A GB21866/55A GB2186655A GB786305A GB 786305 A GB786305 A GB 786305A GB 21866/55 A GB21866/55 A GB 21866/55A GB 2186655 A GB2186655 A GB 2186655A GB 786305 A GB786305 A GB 786305A
- Authority
- GB
- United Kingdom
- Prior art keywords
- benzene
- cumene
- diisopropyl
- catalyst
- per cent
- 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
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C5/00—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms
- C07C5/22—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by isomerisation
- C07C5/27—Rearrangement of carbon atoms in the hydrocarbon skeleton
- C07C5/2729—Changing the branching point of an open chain or the point of substitution on a ring
- C07C5/2732—Catalytic processes
- C07C5/274—Catalytic processes with inorganic acids; with salts or anhydrides of acids
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
Diisopropyl benzene or a mixture of diisopropyl benzene isomers is isomerized by passing in the liquid phase over an aluminium silicate catalyst at 100-300 DEG C. The catalyst may consist of silicates formed from silica and smaller amounts of alumina and of oxides of other metals such as iron, zirconium, magnesium, calcium, sodium and potassium, and of oxides of hydrogen, carbon and sulphur. The catalyst may consist of 85-90 per cent SiO2 and 15-10 per cent Al2O3. The catalyst preferably contains less than 3.5 per cent of water. The process may be carried out at a pressure of 10-80 atm. and preferably less than 5 parts by volume of liquid reactants are passed through each part of the reaction zone per hour. The process may be carried out by alkylating benzene, cumene or mixtures thereof with propene, distilling from the reaction mixture the fraction containing o- and m-diisopropyl benzene and isomerizing this fraction to obtain benzene, cumene, o-, m- and p-diisopropyl benzenes and higher alkylates. The o-isomer is practically completely converted and the m-and p-isomers can be separated by distillation. The benzene and cumene formed may be recycled to the alkylation process; the higher alkylates may either be dealkylated or trans-alkylated with benzene and cumene and the p-isomer separated from the diisopropyl benzenes formed in each case. Specifications 749,186 and 749,187 are referred to.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
NL786305X | 1954-07-30 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB786305A true GB786305A (en) | 1957-11-13 |
Family
ID=19832288
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB21866/55A Expired GB786305A (en) | 1954-07-30 | 1955-07-28 | A process for isomerizing dialkyl benzenes in the liquid phase |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB786305A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US7361798B2 (en) | 2003-10-03 | 2008-04-22 | Exxonmobil Chemical Patents Inc. | Production of dialkylbenzenes |
-
1955
- 1955-07-28 GB GB21866/55A patent/GB786305A/en not_active Expired
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US7361798B2 (en) | 2003-10-03 | 2008-04-22 | Exxonmobil Chemical Patents Inc. | Production of dialkylbenzenes |
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