Purification process of monofluoromethane
A monofluoromethane and process technology, which is applied in the field of monofluoromethane purification process, can solve the problems of easy failure of adsorbent after repeated activation, easy saturation of adsorbent, and unqualified products, so as to maintain stable quality, reduce purification pressure, and ensure The effect of stability
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Embodiment 1
[0063] A kind of monofluoromethane purification process of the present embodiment, comprises the following steps:
[0064] (1), preliminary adsorption: make the monofluoromethane to be purified pass through activated alumina, 5A molecular sieve and 3A molecular sieve successively to carry out preliminary removal of impurities;
[0065] (2), feed and purification: rectifying tower comprises two rectifying tower A and rectifying tower B,
[0066] a. The monofluoromethane to be purified after preliminary adsorption enters the rectification tower A that has been cooled, and rectifies under the conditions of operating pressure of 0.5-0.6Mpa and temperature of -38°C--40°C, and 0.1-0.13kg / h speed discharges the crude product containing light components from the tower top gas phase of rectifying tower A, stops discharging until the light component content in the gas phase detects qualified, and the light components in the monofluoromethane to be purified include carbon dioxide;
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Embodiment 2
[0070] A kind of monofluoromethane purification process of the present embodiment is basically the same as that of embodiment 1, the difference is that in step (2) a, the rectifying tower A is operated at a pressure of 0.6-0.7Mpa and a temperature of -30°C--35°C Carry out rectification under the condition of rectifying tower A with 0.15-0.0.18kg / h speed discharge the crude product containing light components from the tower top gas phase of rectifying tower A; Step (2) b, material in rectifying tower A is with 4kg The / h speed gas phase presses material to rectifying tower B, and stops pressing when the remaining 1 / 10 of the total mass of the substance in rectifying tower A.
Embodiment 3
[0072] A kind of monofluoromethane purification process of the present embodiment is basically the same as that of embodiment 1, the difference is that in step (2) a, the rectifying tower A is operated at a pressure of 0.7-0.8Mpa and a temperature of -20°C--25°C Carry out rectification under the condition of rectifying tower A with 0.18-0.2kg / h speed discharge the thick product containing light components from the tower top gas phase of rectifying tower A; Step (2) b, material in rectifying tower A is with 5kg / h The gas phase presses material to rectifying tower B at speed h, and stops pressing when the remaining total mass of the substance in rectifying tower A is 1 / 8.
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