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May I ask what the reasonable range for the height-to-diameter ratio of a distillation tower is? The distillation tower I calculated for an annual production of 800,000 tons of methanol, with a diameter of 7 meters and a height of 27 meters – is that reasonable?
It is necessary to know what type of trays are used, the parameters of those trays, as well as the type of packing and its parameters; in addition, information on the feed rate and feed composition is required, along with a range of other data needed for calculations
So, what is the reasonable range for the height-to-diameter ratio of a distillation tower?
The tower height is determined by the separation precision, and the tower diameter is determined by the load capacity. Are there any regulations in books or textbooks regarding the height-to-diameter ratio of the tower?
What other conditions are needed? Under certain conditions, the distillation tower I designed looks like this; I want to know whether it is feasible
The tower height is determined by the separation accuracy, while the tower diameter is determined by the load capacity; there are many factors to consider, and it is necessary to determine a relatively reasonable and economical height-to-diameter ratio.
Well, thank you. I’ll ask our teacher whether my design is reasonable The teacher said that as long as the height-to-diameter ratio of the tower is within a reasonable range, it is acceptable. That’s why I asked about the reasonable range for the height-to-diameter ratio. May I add your contact information? My WeChat ID is 361091559.
This one is a bit short and chubby; it doesn’t look like a tower, but rather like a reactor.
The tower diameter has basically no relation to the tower height; it is the length-to-diameter ratio of the container that matters.