A kind of technology and equipment for preparing bromoethane
A technology for bromoethane and equipment, which is applied in the field of technology and equipment for preparing bromoethane, can solve the problems of single mixing structure and inability to combine gas mixing structures, and achieves the effects of improving heating efficiency and smooth spray holes
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Embodiment 1
[0058] as attached figure 1 to the attached Figure 8 shown:
[0059] The present invention provides a process and equipment for preparing bromoethane, comprising a box body 1;
[0060] Box 1 is a rectangular box-like structure;
[0061] Heating structure 2, the heating structure 2 is installed in the box body 1;
[0062] The driving structure 3 is installed on the box body 1 .
[0063] refer to as figure 2 , Box 1 includes:
[0064] Cover plate 102, the cover plate 102 is a rectangular plate-like structure, and the cover plate 102 is fixedly connected to the box body 1 by bolts;
[0065] The protective seat 101, the protective seat 101 is welded on the box body 1, and the protective seat 101 is a back-shaped structure, and the inner wall of the protective seat 101 is in contact with the front, rear, left and right end surfaces of the cover plate 102, so that the cover can be improved. The sealing performance between the plate 102 and the box body 1 .
[0066] refer t...
Embodiment 2
[0093] A process for preparing bromoethane, comprising the following steps:
[0094] 01. Feeding: Pump ethanol and hydrobromic acid from the storage tank area into the closed intermediate tank of the workshop, and meter it into the box 1;
[0095] 02. Reaction and primary rectification: pump quantitative 95% ethanol and quantitative 40% hydrobromic acid into box 1, stir for 0.5 hours, pump into preheater, preheat to the set temperature, and then enter into reactive distillation The tower reacts. The reactive rectification tower is heated to 40 ℃ to carry out a rectification, the temperature of the tower still is 60 degrees, the temperature of the top of the tower is 40 degrees, and the reflux temperature is 15 degrees. The excess hydrobromic acid solution is pumped into the acid recovery tower for distillation and recovery of hydrobromic acid, and the distillation waste liquid of the acid recovery tower is pumped into the waste liquid neutralization kettle.
[0096] 03. Cond...
Embodiment 3
[0100] A process for preparing bromoethane, comprising the following steps:
[0101] 01. Feeding: Pump ethanol and hydrobromic acid from the storage tank area into the closed intermediate tank of the workshop, and meter it into the box 1;
[0102] 02. Reaction and primary rectification: pump quantitative 95% ethanol and quantitative 40% hydrobromic acid into box 1, stir for 0.5 hours, pump into preheater, preheat to the set temperature, and then enter into reactive distillation The tower reacts. The reactive rectification tower is heated to 40 ℃ to carry out a rectification, the temperature of the tower still is 70 degrees, the temperature of the top of the tower is 45 degrees, and the reflux temperature is 15 degrees. The excess hydrobromic acid solution is pumped into the acid recovery tower for distillation and recovery of hydrobromic acid, and the distillation waste liquid of the acid recovery tower is pumped into the waste liquid neutralization kettle.
[0103]03. Conde...
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Abstract
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