Separation method of hexafluoropropylene and monochlorodifluoromethane (F22) mixture
A technology of difluoromonochloromethane and hexafluoropropylene, which is applied in the directions of absorption purification/separation, organic chemistry, etc., can solve the problems of secondary pollution of waste solvent, complicated process flow, and large amount of entrained solvent, and achieve the effect of environmental friendliness
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Embodiment 1
[0046] Will F 22 ~C 3 f 6 The azeotrope (containing 83.88% by volume of F 22 and 16.12 volume percent C 3 f 6 ) is sent to the absorption equipment (2) at a flow rate of 100Kg / h, and the circulating water circulating from the desorption equipment is sent to the upper part of the absorption equipment (2) at a flow rate of 10,000kg / h, so that the circulating water absorbs F22, and the absorption equipment (2) The model is DN150mm×4000mm, the operating temperature is 40°C, and the pressure is 0.45MPa.
[0047] the absorbed F 22 The water is taken out from the bottom of the absorption device (2) and sent to the desorption device (3) for desorption, and the water separated from the top of the desorption device (3) is expressed as F 22 The main mixture is sent back to the cracked gas storage tank. The model of the desorption device (3) is DN150mm×4000mm, the operating pressure is 0.02MPa, and the temperature is 70°C.
[0048] Send the gas that has been absorbed and washed on...
Embodiment 2
[0055] Will F 22 ~C 3 f 6 The azeotrope (containing 83.88% by volume of F 22 and 16.12 volume percent C 3 f 6 ) is sent to the absorption equipment (2) with a flow rate of 100Kg / h, and the deionized water circulating from the desorption equipment is sent to the top of the absorption equipment (2) with a flow rate of 10000kg / h, so that the deionized water absorbs F22, absorbs The model of the equipment (2) is DN150mm×4000mm, the operating temperature is 40°C, and the pressure is 0.45MPa.
[0056] the absorbed F 22 The deionized water is taken out from the bottom of the absorption device (2) and sent to the desorption device (3) for desorption, and the deionized water separated from the top of the desorption device (3) is desorbed as F 22 The main mixture is sent back to the cracked gas storage tank. The model of the desorption device (3) is DN150mm×4000mm, the operating pressure is 0.02MPa, and the temperature is 70°C.
[0057] The gas that has been absorbed and washed ...
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