A newcomer is begging for guidance; I’ve really thought about it for days without figuring it out – design of sieve plate towers, gas-liquid equilibrium
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I am designing a stripping tower and calculating the phase equilibrium values. However, the m value I obtained results in a very high gas flow rate when used in subsequent calculations, which is not acceptable. I don’t know where the problem lies. I hope someone experienced can see my post and provide feedback; I would be extremely grateful
The density of toluene was incorrect; I have corrected it
But why isn’t there anyone knowledgeable who can help answer the question? It would be great if you could at least tell me the Henry’s law constants for benzene and toluene at 20 degrees Celsius.: