First of all, I'd get all the pneumatic equipment that will go into the plant and obtain their air consumption (that figure should be in the equipment specifications). You add them all up.
Then you calculate how much volume your compressed air piping is going to be. You add a generous amount of fat and you're good to go.
I know that's too vague but I don't want to go into too much detail.
A good pneumatics contractor can do all these calculations for you. I also believe some pneumatics manufacturers (Festo, SMC, Rexroth, etc.) have software that will allow you to do the calculations yourself. I don't think it's free though.
regards,
Vulcan
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First of all, an investigation shall be made to determine air applications(consumers) The applications(consumers) are generally instruments(air
operated valves, …), plant air.
The
total requirement of instrument air depends on the types of process
facilities and instruments installed. Based on existence experience the following can be useful for your request:
1- By rule of thumb, the instrument air requirement can be considered
about 1-1.6 Sm3/h
of dry air for each instrument pilot in process units.
(2)-For a simple process plant(like NGL Recovery),total compressed air=inst. air+plant air
3- Min. plant air consumption is usually about 1/3 times (2)
4- Air leakage of the air generation unit~ 10% to the estimated amount of consumption(3)
5- Considering 25% as Over design capacity
it should be noted that for oil refinery other req. shall be added to (2)
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