floben
Mechanical
- Feb 9, 2013
- 1
Good Day,
My team is evaluating the use of an existing pumping system with new equpment that will require less pressure from the pump. The existing pumps are controlled by VFDs; the first page of the attached curves shows the design point of 632 gpm @ 618'TDH. With new equpment installed, the discharge pressure from the pumps needs to be approximately 208' (same flow). Using the manufacturer's software, it appears the pumps would need to run at I've been however, it appears that meeting the design condition of 632 gpm @ ____' TDH would result in the pump operating at 2,470 rpm to get to the required flow and discharge pressure. It looks as though this condition would cause the pump to run right at the end of it's curve (see attached). My team could use your help with the following questions and any other suggestions you may have:
1) What is likely to happen if the pump runs near the end of it's curve?
2) Does it make any sense to try to add an orifice plate on the discharge piping and to increase the pump speed to get the pump closer to a more efficient operating point?
3) For item 2 above, note that the discharge pressure will vary on a daily basis by about 35 psi or so.
I'm concerned both about operating the pump at the end of its curve, and am just as concerned about tying to mess with having a pressure inducing valve or orifice plate fighting the the VFDs.
Thanks for your time and any help you can offer.
My team is evaluating the use of an existing pumping system with new equpment that will require less pressure from the pump. The existing pumps are controlled by VFDs; the first page of the attached curves shows the design point of 632 gpm @ 618'TDH. With new equpment installed, the discharge pressure from the pumps needs to be approximately 208' (same flow). Using the manufacturer's software, it appears the pumps would need to run at I've been however, it appears that meeting the design condition of 632 gpm @ ____' TDH would result in the pump operating at 2,470 rpm to get to the required flow and discharge pressure. It looks as though this condition would cause the pump to run right at the end of it's curve (see attached). My team could use your help with the following questions and any other suggestions you may have:
1) What is likely to happen if the pump runs near the end of it's curve?
2) Does it make any sense to try to add an orifice plate on the discharge piping and to increase the pump speed to get the pump closer to a more efficient operating point?
3) For item 2 above, note that the discharge pressure will vary on a daily basis by about 35 psi or so.
I'm concerned both about operating the pump at the end of its curve, and am just as concerned about tying to mess with having a pressure inducing valve or orifice plate fighting the the VFDs.
Thanks for your time and any help you can offer.