RRichardson
Civil/Environmental
- Aug 15, 2012
- 10
I have this idea to adapt what is common in storm water practice (vortex separation), to fats, oils and grease screening before being pumped into anaerobic digesters. The only difference is that I have no intention of capturing the volatile stuff, the FOG. The vortex will be used to capture heavy particles, which I suspect will be better than the existing rock baffle.
So I've been pouring over lots of vortex equations trying to size the vertical column pipe. Trucks will empty tanks at about 250 gpm into a 6-inch pipe that will enter tangentially into a vertical column pipe. The 6-inch pipe will be about mid-way. If the vertical pipe is 4 feet in diameter with about 8 feet in elevation head between the truck and vortex separator, I'm estimating the strength of the vortex to be about 0.008 ft^2/s with an elevation difference between the center and outside radius about 1.3 feet. Am I doing this right? Is there a better way to size this column?
So I've been pouring over lots of vortex equations trying to size the vertical column pipe. Trucks will empty tanks at about 250 gpm into a 6-inch pipe that will enter tangentially into a vertical column pipe. The 6-inch pipe will be about mid-way. If the vertical pipe is 4 feet in diameter with about 8 feet in elevation head between the truck and vortex separator, I'm estimating the strength of the vortex to be about 0.008 ft^2/s with an elevation difference between the center and outside radius about 1.3 feet. Am I doing this right? Is there a better way to size this column?