The utility model relates to the technical field of
coal chemical equipment, in particular to a condensation
refrigeration system of a VOCs (volatile organic compounds) treatment device, which comprises a first
heat exchanger tube pass input end connected with a first
liquid phase propylene conveying
branch tube, a tube pass output end connected with a first output
branch tube, a shell pass input end connected with a
refrigerant conveying tube, and a second
heat exchanger tube pass output end connected with a second
liquid phase propylene conveying
branch tube. The shell pass output end is connected with a first
refrigerant output
pipe; the tube pass input end of the second
heat exchanger is connected with a second liquid-phase propylene conveying branch
pipe, the tube pass output end of the second heat exchanger is connected with a second output branch
pipe, the shell pass input end of the second heat exchanger is connected with a first conveying pipe for flowing VOCs and
methanol gas, and the shell pass output end of the second heat exchanger is connected with a second conveying pipe; the tube pass input end of the third heat exchanger is connected with the first
refrigerant output pipe, the tube pass output end is connected with the second refrigerant output pipe, the shell pass input end is connected with the second conveying pipe, and the shell pass output end is connected with the third conveying pipe. According to the utility model, the problems of poor pre-
cooling effect, long driving time and high
power consumption of the compressor are solved.