Can falling film evaporators be calculated in HTRI?
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I have never used a falling film evaporator before; even though the manufacturer has prepared a plan, I don’t know how to verify it. I hope someone experienced can give me some advice
In falling film evaporation, hot gas flows from top to bottom; the pressure drop is low, the temperature difference is large, and thus less cooling water is required
There are hardly any in the domestic market, aside from Sulzer and DB Schenker
It can be calculated, but you need the physical property data, namely those of the evaporating material.