How to calculate the equipment diameter?
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The current conditions are: equipment flow rate of 120,000 NM3/h, pressure of 0.1 MPa, and temperature of 40 degrees Celsius. It is necessary to calculate what diameter the equipment should have Excuse me, expert, how should I calculate it? Are there any empirical formulas to follow? I haven’t been able to solve this problem since I started working in this field half a year ago; I’m seeking advice!
What kind of equipment, storage tanks or buffer tanks, or other towers, etc.?
Is it a device or a pipeline? Is it a gas-phase medium or a liquid-phase medium? Is it an empty tower? Packed tower? Reactor? Buffer tank? If you don’t explain clearly, it will be hard for us to help you.
As a supplementary note: it is a gas-liquid separation device, a vertical container, whose main function is to separate liquids and mist droplets from the gas phase.
If you specify what the medium is and its concentration, we can help you with the design. 0917-3307181 Zhang Jinbo
You can also read books on separators
Well, is it because the condensate water produced by the water ring vacuum pump? Your question is really frustrating. It doesn’t mention the devices at the beginning and end, only those in the middle. First, how much water does your gas carry away per hour? Is the water discharged directly or is it recycled? Once the amount of water is known, can’t the diameter be determined then? Well, isn’t the volume just derived from that? What do you need the diameter for? As long as the output capacity is good and the equipment looks nice, that’s enough; it’s not a standard product anyway!