System for recovering and treating tail gas from nitrile rubber production
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Embodiment 1
[0021] Reactor 1 vent pipe is connected to the first-level washing tower of washing tower 2, and the demulsification device is installed on the first-level washing tower, and the pipe is connected to RTO5 equipment on the demulsification device, the second-level washing tower is connected to the first-level washing tower, and the third-level washing tower is connected to the first-level washing tower. The scrubber is connected to the secondary scrubber, the primary condenser 301 is connected to the tertiary scrubber, the condensation temperature of the primary condenser 301 is 0°C, the secondary condenser 302 is connected to the primary condenser 301, and the secondary condenser The condensation temperature of 302 is -25°C, butadiene recovery tank 4 is installed at the lower end of secondary condenser 302 to recover condensed butadiene, RTO5 is connected with secondary condenser 302, and the number of RTO5 heat storage chambers is 3 , Install a combustion-supporting fan, a wate...
Embodiment 2
[0026] According to the method of Example 1, a kind of nitrile rubber production tail gas recovery treatment system is designed, the difference is that: the condensation temperature of the primary condenser 301 is -5°C, and the condensation temperature of the secondary condenser 302 is -30°C.
Embodiment 3
[0028] According to the method of embodiment 1, design a kind of nitrile rubber production tail gas recycling treatment system, difference is: the quantity of RTO5 regenerator is 5 chambers.
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