Method for continuously diphenyl carbonate
A technology of diphenyl carbonate and dimethyl carbonate, which is applied in the field of continuous production of phenylethyl carbonate, can solve the problems of low yield of diphenyl carbonate and low conversion rate of dimethyl carbonate, etc.
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1
[0031]In a process device mainly composed of a reactive distillation tower, a phenyl acetate separation tower and a diphenyl carbonate separation tower, the raw materials dimethyl carbonate and phenyl acetate are prepared under the action of catalyst butyl titanate to produce dicarbonate phenyl esters.
[0032] The reactive distillation tower is a plate tower with a diameter of 300mm and a height of 16000mm, with 30 trays inside; the phenyl acetate separation tower is a packed tower with a diameter of 300mm and a height of 12000mm, with structured packing inside, and the number of theoretical plates is 40; The diphenyl ester separation tower is a packed tower with a diameter of 200mm and a height of 8000mm, with structured packing inside, and the number of theoretical plates is 20.
[0033] Reactive distillation column operating conditions:
[0034] Raw material dimethyl carbonate enters the lower part of the reactive distillation column at a rate of 9kg / h, phenyl acetate is ...
Embodiment 2
[0038] In a process device mainly composed of a reactive distillation tower, a phenyl acetate separation tower, and a diphenyl carbonate separation tower, the raw materials dimethyl carbonate and phenyl acetate are produced under the action of a catalyst dibutyltin oxide Diphenyl carbonate.
[0039] The reactive distillation tower is a packed tower with a diameter of 300 mm and a height of 30,000 mm, with a built-in structured packing of 25 m and a theoretical plate number of 80;
[0040] Reactive distillation column operating conditions
[0041] The catalyst is dibutyltin oxide (dissolved in phenyl acetate in advance), and the feed amount of raw materials and catalyst is the same as in Example 1. The reflux ratio at the top of the tower is 2, the temperature at the bottom of the tower is 216-219°C, and the temperature at the top of the tower is 62-64°C. The discharge amount at the top of the tower is 13.6kg / h, and it is composed of methyl acetate, which is discharged outsid...
PUM
| Property | Measurement | Unit |
|---|---|---|
| diameter | aaaaa | aaaaa |
| diameter | aaaaa | aaaaa |
Abstract
Description
Claims
Application Information
Login to View More 


