A waste gas treatment method for a reaction process of preparing epoxy chloropropane from chloropropene
An epichlorohydrin and chloropropene technology, applied in the disproportionation separation/purification of halogenated hydrocarbons, organic chemistry, etc., can solve the problems of chloropropene loss, air pollution, etc. Effect
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Embodiment 1
[0018] Set the temperature of the tower bottom heat exchanger E1 to 10°C;
[0019] Set the temperature of the top condenser E2 heat exchanger to -15°C;
[0020] Set the pressure range of absorption tower T1 as: 100kPa,
[0021] The filling amount of epichlorohydrin in the tower bottom of the absorption tower T1 is set to be 50% of the volume of the tower bottom.
[0022] Using hydrogen peroxide as the oxygen source, the reaction-controlled phase transfer catalyst catalyzes the epoxidation of chloropropene to prepare epichlorohydrin. The results of waste gas treatment in the reaction process are shown in Table 1. It can be seen that the organic matter in the waste gas after this process is greatly reduced, reducing the The content of allyl chloride in the exhaust gas.
[0023] Table 1. Waste gas treatment results of the epoxidation of propylene chloride to prepare epichlorohydrin
[0024]
Embodiment 2
[0026] Set the temperature of the tower bottom heat exchanger E1 to 0°C;
[0027] Set the temperature of the top condenser E2 heat exchanger to -20°C;
[0028] Set the pressure range of absorption tower T1 as: 500kPa,
[0029] The filling amount of epichlorohydrin in the tower bottom of the absorption tower T1 is set to be 65% of the volume of the tower bottom.
[0030] Using hydrogen peroxide as the oxygen source, the reaction-controlled phase transfer catalyst catalyzes the epoxidation of chloropropene to prepare epichlorohydrin. The results of waste gas treatment in the reaction process are shown in Table 2. It can be seen that the organic matter in the waste gas after this process is greatly reduced, reducing the The content of allyl chloride in the exhaust gas.
[0031] Table 2. Waste gas treatment results of the epoxidation of propylene chloride to prepare epichlorohydrin
[0032]
Embodiment 3
[0034] Set the temperature of the tower bottom heat exchanger E1 to 15°C;
[0035] Set the temperature of the top condenser E2 heat exchanger to -10°C;
[0036] Set the pressure range of absorption tower T1 as: 300kPa,
[0037] The filling amount of epichlorohydrin in the tower bottom of the absorption tower T1 is set to be 45% of the volume of the tower bottom.
[0038] Using hydrogen peroxide as the oxygen source, the reaction-controlled phase transfer catalyst catalyzes the epoxidation of chloropropene to prepare epichlorohydrin. The results of waste gas treatment in the reaction process are shown in Table 3. It can be seen that the organic matter in the waste gas after this process is greatly reduced, reducing the The content of allyl chloride in the exhaust gas.
[0039] Table 3. Waste gas treatment results of the epoxidation of propylene chloride to prepare epichlorohydrin
[0040]
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