Calculate the nitrogen consumption for the electrostatic tar catcher
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What is the typical nitrogen consumption for an electrostatic tar catcher? (Treatment capacity: 30,000 units per hour)
80-120 cubic meters per hour
It is related to the electrostatic capture structure as well as process operations; mainly, nitrogen is used for starting up and shutting down the system. During normal operation, it is sufficient to maintain the temperature and pressure inside the insulation box ~90-110℃
I checked the previous preliminary designs; for an electrostatic precipitator with a capacity of 1 million tons, the nitrogen flow rate for the protective insulation box is 3 cubic meters per minute. This is roughly the same as what was mentioned on the second floor. Thank you to everyone.
The parameters for a single electric precipitator are 50-80 cubic meters per hour
30,000 – roughly 40–60 m3/h I guess
:lol :lol :lol The electrostatic tar catcher in my factory is of the QS-F220-11 type; it hasn’t yet been equipped with nitrogen supply
The main role of nitrogen during the operation of the electrostatic precipitator is to prevent gas from entering the insulation box; the specific amount required must be determined based on the actual conditions on site. Our capacity is 50-60 m3/h; it is generally not adjusted based on the amount of gas used
Is this amount using canned gas, and what size of canned gas?