A factory has two production lines, the main product is 200L drums, the annual output of 1.3 million in the production process due to the use of toluene-containing paint, paint and drying process in the production of "triphenyl" emissions, polluting the surrounding Of the environment; for the organic waste gas with a large amount of wind, low concentration characteristics of the plant in 2010 using
Activated Carbon fiber adsorption - catalytic combustion of new devices to deal with "triphenyl" exhaust gas, air volume of 1800m3 / h.
In order to ensure the continuous operation of the system, the adsorber adopts a multi-unit shunt combined structure. In normal operation, there is only one unit in desorption state while the other units are in adsorption or cooling state. Organic waste gas is collected and then enters the n-1 A unit of adsorption, the purified gas into the atmosphere. Before normal adsorption, the catalytic bed combustion chamber is first preheated to 300 ° C. After a certain period of time, when the activated
Carbon fibers in one unit are saturated, the desorption valve is opened and desorbed by hot air at 120 ° C. The desorbed high concentration Organic waste gas into the catalytic bed combustion decomposition of CO2 and H2O, purified high-temperature gas through the tube heat exchanger to preheat the desorption of gas, a small part of the discharge through the chimney, the rest of the fresh air after the return hot air as desorption, this time Stop electric heater preheating, and through the vent valve and make up the cooling fan to achieve the entire catalytic combustion system thermal balance. Each unit adsorption and desorption butterfly pneumatic valve by PLC industrial computer programmable controller according to set the time difference orderly switch, the entire electronic control device sub-manual and automatic two groups, and with automatic alarm system.
