foodprojengr
Chemical
- Jun 25, 2008
- 45
My project involves providing my maintenance person specs to run piping from a 3hp air compressor and dryer to a propietary machine and from a water softener to a vacuum pump (for cooling water) to that same propietary machine. The air compressor can provide up to 10 cfm at max pressure (see and Based on this, I was planning on running a 1" ID PVC line for the compressed air and a 1/2" ID PVC line for the soft water from the water softener to the vacuum pump and from the pump to the drain, as well as from the water softener to the drain for when it regenerates.
The vacuum pump requires 1 L/min cooling water = 0.26 gal/min = 60 cuin/min). I assumed a max flow rate of 5 ft/sec and calculated a minimum diamter of 0.15 in. I sized it up to 1/2" ID for safety.
I know I need to also consider temperature and pressure. The water from the softener should be room temp and the plant water supplying the water softener is 60 psi.
For the compressed air, I also assumed 5 ft/sec maximum flow rate and using the max 10 cfm I calculated 1.2 in.
I'm not sure what to consider for pressure and temp for the compressed air.
I'm choosing PVC because of a tight budget and the fact that the client may be adding more machines in the future and so we'll have to resize the line anyway.
Does this make sense?
I'm obviously new at spec'ing piping so sorry for the dumb question.
The vacuum pump requires 1 L/min cooling water = 0.26 gal/min = 60 cuin/min). I assumed a max flow rate of 5 ft/sec and calculated a minimum diamter of 0.15 in. I sized it up to 1/2" ID for safety.
I know I need to also consider temperature and pressure. The water from the softener should be room temp and the plant water supplying the water softener is 60 psi.
For the compressed air, I also assumed 5 ft/sec maximum flow rate and using the max 10 cfm I calculated 1.2 in.
I'm not sure what to consider for pressure and temp for the compressed air.
I'm choosing PVC because of a tight budget and the fact that the client may be adding more machines in the future and so we'll have to resize the line anyway.
Does this make sense?
I'm obviously new at spec'ing piping so sorry for the dumb question.