Method for producing 1,3-dioxolane based on reaction-separation coupling
A technology of dioxolane and reaction, which is applied in the direction of organic chemistry, can solve the problems of increasing energy consumption and increasing costs, and achieves the effects of convenient operation, simple equipment, and cost reduction
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1
[0029] Embodiment 1, figure 1 A circulating pressurized reaction-rectification coupling device is given, including ethylene glycol raw material tank 1, formaldehyde raw material tank 7, feed pump 2, feed pump 37, absorption tower 3, reactive distillation tower 4, condensation Device 6 and reboiler 25 etc.
[0030] A material inlet and a liquid outlet are respectively provided at the bottom of the reactive distillation tower 4 , a side line outlet is arranged at the middle of the reactive distillation tower 4 , and a gas outlet is arranged at the top of the reactive distillation tower 4 .
[0031] The ethylene glycol raw material tank 1 is connected to the inlet of the feed pump 2 through the feed pipe 9, and a shut-off valve 10 is arranged on the feed pipe 9; the outlet of the feed pump 2 is connected to the feed pipe 27. The formaldehyde raw material tank 7 is connected to the inlet of the feed pump 37 through the feed pipe 35, and a stop valve 36 is arranged on the feed pip...
Embodiment 2
[0037] Embodiment 2, a method for producing 1,3-dioxolane based on reaction-separation coupling, using the device described in Embodiment 1, the following steps are carried out in sequence:
[0038] 1), preparatory work:
[0039] There is ethylene glycol in ethylene glycol raw material tank 1; Store 30% (volume concentration) formaldehyde solution in formaldehyde raw material tank 7; Store in advance by 30% (volume concentration) formaldehyde solution and ethyl alcohol at the bottom of reactive distillation column 4 600 mL of raw material composed of diol (the molar ratio of formaldehyde to ethylene glycol is 1:1). Place filler γ-Al at the bottom of reactive distillation column 4 2 o 3 (S BET =275m 2 / g, aperture 4.68nm) 20g, γ-Al is set in the middle part of reactive distillation tower 4 2 o 3 About 300ml.
[0040] γ-Al at the bottom of reactive distillation column 4 2 o 3 It only acts as a reaction catalyst, and the γ-Al located in the middle of the reaction distill...
Embodiment 2~ Embodiment 4
[0060] Change the following reaction conditions among the embodiment 1: the feed rate r of raw material ethylene glycol, the heating power Q of the tower top pressure P of reactive distillation column 4, reboiler 25 and the setting in reactive distillation column 4 Catalyst type, obtain embodiment 2~4, specific data see table 1.
[0061] Table 1, embodiment 2~4 data
[0062]
PUM
| Property | Measurement | Unit |
|---|---|---|
| height | aaaaa | aaaaa |
| height | aaaaa | aaaaa |
| pore size | aaaaa | aaaaa |
Abstract
Description
Claims
Application Information
Login to View More 