Hello,
I have a 140F water distribution loop that spans my plant with a discharge pump and buffer tank. The distribution line is 1.37" id and has a discharge pressure of 100 psi at the pump outlet as well as a static (no consumption) return pressure of 25 which is regulated with a back-pressure valve. The loop has multiple 0.87" id points-of-use "tees" that I have recently choked to limit use flow. I was wondering what is the theoretical method for calculating the flow rate from a Point-of-use "tee" assuming no choking of additional orifice other than the reduction of the "tee's"s diameter. We can assume the pressure at the point of use for the example would be 70 (after -30psi due to equivalent length and exchangers). Let's assume only this point would be used.
I am sure this has been discussed and I did try to find it however they all reduce to orifice calculations, which I don't think apply because my case involves a distribution loop and some flow will not pass through the point-of-use orifice (tee). Right?? even a point in the right direction would be appreciated.
Thanks,
John
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