An integrated production platform for chlorinated polymers
A technology of chlorinated polymer and production platform, applied in chemical/physical/physical-chemical stationary reactors, chemical/physical processes, methods of chemically changing substances by atmospheric pressure, etc., to reduce production costs and improve Product adjustment ability and market adaptability, the effect of improving production efficiency and utilization rate
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Embodiment 1
[0041] 1. Design of chlorination reaction kettle: the selected chlorination reaction kettle is 25m 3 A glass-lined kettle, the top of the chlorination reaction kettle is provided with a liquid chlorine feed port 1, the blade of the agitator 4 provided in the reaction kettle is a three-blade back-sweeping type, three stirring layers, and the top stirring layer The distance h from the middle stirring layer 3 850mm; the distance h between the middle stirring layer and the bottom stirring layer 2 850mm; the distance between the bottom stirring layer and the bottom of the tank h 1 is 250mm; the ratio d / D of the diameter d of the stirred layer to the internal diameter D of the reactor is 0.6, and the height-to-diameter ratio (H / D) of the chlorination kettle is 1.87;
[0042] The bottom of the chlorination reactor is provided with a gas chlorine feed port 2 and a discharge port 3 . The gas chlorine feed port 2 is an eccentric design, and its eccentricity r=d / 3.
[0043] 2. Chlori...
Embodiment 2
[0054] 1, chlorination reactor design: the chlorination reactor selected is the same as embodiment 1.
[0055] 2. Chlorination process: The raw material PP resin enters the chlorination reaction kettle for chlorination reaction. The initial temperature of the chlorination reaction is 50°C and normal pressure. When the chlorination reaction ends, the temperature is 110°C and the pressure is 0.35MPa. ; After the chlorination reaction is completed, the material enters the multifunctional quick separation device after coming out of the discharge port 3;
[0056] 3. Separation process:
[0057] (A) the CPP material to be separated enters the deconcentrated acid zone to remove hydrogen ions, and the feed rate of the CPP material is controlled by the separated concentrated hydrochloric acid flow ratio; the volume flow rate of the concentrated hydrochloric acid / material feed volume flow ratio is 0.7, The vacuum degree of the acid deconcentration zone is 0.005-0.01MPa (absolute pressu...
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