zabrab
Civil/Environmental
- Jan 7, 2006
- 41
I am reviewing a design for a duplex grinder pump station to serve 25 homes.
Looking back over my experience, it has really not included this type of application. My experience has been in projects that the same size and larger using non-clog pumps and grinder pump projects that are much smaller (grinders for one or two homes or a commercial establishment).
Way way back in my mind (I’m thinking the mid 1980s section), I seem to recall that when sizing a grinder pump station for a larger multiple home application, in addition to hydraulic considerations, there were manufacturer recommendations or even limitations on the number of homes that should connected to the station.
I haven’t seen anything in the current catalogs and In lunchtime chatter I’ve asked a couple of colleagues and they have never heard of this.
Has anyone heard of this type of limitation? If there is one, what is the basis for it? I presume it would be due to the shredding operation.
When we were kicking this around the table at lunch, the consensus solution was the pragmatic consideration of force main diameter. If you can use a 1-1/2” or 2” diameter force main, use grinder pumps, if your force main diameter is 3” or 4” for hydraulics, go to non-clog pumps.
What considerations do you use considering grinder pumps vs non-clog pumps?
Looking back over my experience, it has really not included this type of application. My experience has been in projects that the same size and larger using non-clog pumps and grinder pump projects that are much smaller (grinders for one or two homes or a commercial establishment).
Way way back in my mind (I’m thinking the mid 1980s section), I seem to recall that when sizing a grinder pump station for a larger multiple home application, in addition to hydraulic considerations, there were manufacturer recommendations or even limitations on the number of homes that should connected to the station.
I haven’t seen anything in the current catalogs and In lunchtime chatter I’ve asked a couple of colleagues and they have never heard of this.
Has anyone heard of this type of limitation? If there is one, what is the basis for it? I presume it would be due to the shredding operation.
When we were kicking this around the table at lunch, the consensus solution was the pragmatic consideration of force main diameter. If you can use a 1-1/2” or 2” diameter force main, use grinder pumps, if your force main diameter is 3” or 4” for hydraulics, go to non-clog pumps.
What considerations do you use considering grinder pumps vs non-clog pumps?