uartsims
Civil/Environmental
- Dec 29, 2004
- 1
Hey guys. Wanted to get a few thoughts on this situation. I have a client who has a small sanitary sewer pump station designed for a residential development. To make a long story short, he has expanded the subdivision a couple of different times and now the station is inadequate for the anticipated flows.
Currently, the station is pumping approx. 40 gpm based on recent field tests we conducted. The required flow (based on peak conditions) is about 90 gpm. The simple solution here (and maybe the only one) is to replace the system. However, upon review and in the interest of my client, I have discovered an unusual piping configuration for the discharge line(s). A 4" line runs from the station for about 1000', then necks down to a 3" line for about 1200', then connects to an 8" force main about 920' long, and finally to a 4535' 12" line that makes its way to the treatment plant. Friction losses in the discharge pipe system equate to about 1/2 of the TDH.
I have found an alternate route for the discharge system in which a line from the pump station could be connected directly into the last leg of the 12" discharge pipe that empties into the treatment plant. This alternate route bypasses approximately 3300 lf of pipe. However, my dilemma stems from the fact that a 4" discharge line still doesn't quite allow the required flow from the pumps. But, if the line was increased to a 6" force main instead, the design flow would meet the requirements to obtain 90 gpm flow.
Has anyone ever encountered adjusting discharge pipe sizing solely to modify anticipated friction head losses? Is this a good idea? Laying another 1,000 lf of 6" discharge line would certainly be less expensive than upgrading the existing pump station to accomodate the existing configuration. ANy thoughts? Thanks in advance.
Currently, the station is pumping approx. 40 gpm based on recent field tests we conducted. The required flow (based on peak conditions) is about 90 gpm. The simple solution here (and maybe the only one) is to replace the system. However, upon review and in the interest of my client, I have discovered an unusual piping configuration for the discharge line(s). A 4" line runs from the station for about 1000', then necks down to a 3" line for about 1200', then connects to an 8" force main about 920' long, and finally to a 4535' 12" line that makes its way to the treatment plant. Friction losses in the discharge pipe system equate to about 1/2 of the TDH.
I have found an alternate route for the discharge system in which a line from the pump station could be connected directly into the last leg of the 12" discharge pipe that empties into the treatment plant. This alternate route bypasses approximately 3300 lf of pipe. However, my dilemma stems from the fact that a 4" discharge line still doesn't quite allow the required flow from the pumps. But, if the line was increased to a 6" force main instead, the design flow would meet the requirements to obtain 90 gpm flow.
Has anyone ever encountered adjusting discharge pipe sizing solely to modify anticipated friction head losses? Is this a good idea? Laying another 1,000 lf of 6" discharge line would certainly be less expensive than upgrading the existing pump station to accomodate the existing configuration. ANy thoughts? Thanks in advance.