Preparation process and apparatus of high concentration anhydrous HBr/CH3 COOH agent
A high-concentration, reagent-based technology, applied in chemical instruments and methods, physical/chemical process catalysts, organic compound/hydride/coordination complex catalysts, etc., can solve increased processing difficulty, high cost, product quality and output limitations and other problems, to achieve the effect of preventing the reverse diffusion of water vapor, slowing down the reaction speed and strong dissolving ability
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Embodiment 1
[0014] Such as figure 1 As shown, the device of the present invention comprises a gas generating device composed of a temperature controller 1 with a water bath device, a reaction tank 2, a constant pressure dropping funnel 3, an agitator 4, and a reflux condenser tube 5, and two connecting pipes are connected. Purification tanks 6 and 7, the two ends of the connecting pipe are close to the bottom of the tank, the purification tank 7 is connected with the gas absorption tank 9 through the communication pipe and the buffer bottle 8, a water bath 10 is arranged outside the absorption tank, and the gas absorption tank is connected to the double-stage drying tank through the connecting pipe. The towers 11 and 12 are connected, and the double-stage drying tower is connected with the tail gas absorption tower 13 . The two ends of each connecting pipe are preferably close to the bottom of the tank. The specific preparation method is as follows:
[0015] 1. Preparation of anhydrous ...
Embodiment 2
[0019] Embodiment 2: device is the same as embodiment 1, and concrete preparation method is as follows:
[0020] 1. Preparation of anhydrous acetic acid: freeze glacial acetic acid at 10°C, then pour or filter to remove unfrozen liquid, then melt in a warm water bath, transfer to a reflux distillation device and add 1.0% of the total weight of glacial acetic acid P 2 o 5 , and the reflux distillation unit was filled with molten solid KOH and anhydrous CaCl respectively 2 The two-stage drying tower is connected, and the reflux is distilled after 3 hours to obtain anhydrous acetic acid.
[0021] 2. Add 30 parts by weight of red phosphorus, CCl 4 35 parts by weight, 90 parts by weight of hydrobromic acid of 45%, respectively add 85% H to two scrubbing tanks 3 PO 4 35 parts by weight, P 2 o 5 4 parts by weight, 4 parts by weight of red phosphorus, add 110 parts by weight of anhydrous acetic acid to the absorption tank, successively connect the reaction tank (one end of the r...
Embodiment 3
[0024] Embodiment 3: device is the same as embodiment 1, and concrete preparation method is as follows:
[0025] 1. Preparation of anhydrous acetic acid: freeze glacial acetic acid at 6°C, then pour or filter to remove the unfrozen liquid, then melt it in a warm water bath, transfer to a reflux distillation device and add 0.9% of the total weight of glacial acetic acid P 2 o 5 , and the reflux distillation unit was filled with molten solid KOH and anhydrous CaCl respectively 2 The two-stage drying tower is connected, and the reflux is distilled after 2.5 hours to obtain anhydrous acetic acid.
[0026]2. Add 30 parts by weight of red phosphorus, CCl 4 30 parts by weight, 80 parts by weight of hydrobromic acid of 45%, respectively add 85%H to two scrubbing tanks 3 PO 4 30 parts by weight, P 2 o 5 5 parts by weight, 3 parts by weight of red phosphorus, add 100 parts by weight of anhydrous acetic acid to the absorption tank, successively connect the reaction tank (one end of...
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