Production method of synthesizing HCFC-151a by using chloroethylene
A production method and technology of vinyl chloride, applied in the direction of halogen addition preparation, organic chemistry, etc., can solve the problems of shortage of raw materials and high production cost
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Embodiment 1
[0027] According to the above process flow and steps, 1Kg TiCl is charged in the 50L reactor 1 4 And put in 1.5Kg of AHF for activation for 5 hours, then put in 10Kg of AHF and 10Kg of VCM, control the reaction temperature at about 15°C, and control the reaction pressure at 0.20-0.4Mpa. Half an hour later, reaction kettle 1 gas phase sampling chromatographic analysis gave the composition of the crude product shown in Table 1.
[0028] Table I
[0029]
[0030] Conclusion: CH can be calculated from the data in Table 1 2 = The selectivity of converting CHCl to HCFC-151a is 89.6%, and the selectivity of finally converting CFC-151a and HFC-152a is 99.92%.
Embodiment 2
[0032] According to the above process flow and steps, 1Kg TiCl is charged in the 50L reactor 1 4 And put in 1.5Kg of HF to activate for 5 hours, then put in 5Kg of AHF and 10Kg of VCM at the same time, control the reaction temperature at about 15°C, and control the reaction pressure at 0.20-0.4Mpa. Half an hour later, reaction kettle 1 gas phase sampling chromatographic analysis gave the composition of the crude product shown in Table 2. Table II
[0033]
[0034] Conclusion: CH can be calculated from the data in Table 2 2 = The selectivity of CHCl to HCFC-151a is 91.85%, and the selectivity of final conversion to HCFC-151a and HFC-152a is 99.36%.
Embodiment 3、4
[0036] According to the operating steps of Example 1, the reaction is carried out under the reaction conditions of temperature 3~8°C, pressure 0.05~0.1Mpa and temperature 40~45°C, pressure 0.6~0.8Mpa, and other conditions are constant, and the reaction crude product sampling chromatographic analysis gives The composition of the crude product is shown in Table 3. Table three
[0037]
[0038] Conclusion: The above data show that when the reaction is carried out at a temperature lower than 10°C, the conversion of VCM is not complete; when the reaction is carried out at a temperature greater than 40°C, the amount of high boilers generated increases; therefore, the optimum reaction temperature is 10-35 ℃.
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