How to calculate the desorption air volume for adsorption-catalytic combustion of organic waste gases
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As the title suggests, I would like to ask: how is the desorption air volume calculated, and how should the desorption fan be selected??? At present, I only have a rough idea of the lower limit for 1/4 explosion pressure; how exactly is it calculated? ? Seeking advice! ! !
What specific operating conditions? It depends on the amount you need for regeneration; generally, the required amount is determined by factors such as the regeneration time. It’s similar to molecular sieve adsorption, I guess!
The regeneration time is 5-6 hours, and then… I can’t calculate it. . . .
You need to describe your relevant processes so that it’s possible to determine how to carry out the calculations; it’s nothing more than energy accounting, but it’s important to know what makes up those processes. It’s hard to say right now!
The volume of the activated carbon adsorption tank is 10 m3; it uses honeycomb activated carbon. The amount of adsorption capacity is not clear. Based on the saturated adsorption capacity, thermal air is used for desorption, and after desorption, the material goes into a catalytic combustion unit. That’s all for now. Is it possible to calculate it? If not, what other parameters are needed?
The volume of the activated carbon adsorption tank is 10 m3; it uses honeycomb activated carbon. What about the concentration and flow rate of the waste gas?