I've been told by several folks that the threshold for salt in an activated sludge process is 8 parts per thousand. Actually there were a range of numbers presented, but 8 seemed to be on the lower end of the threshold. That said, I've performed the subsequent calculation like this:
There are essentially three stages of regeneration:
1) Backwash: 4gpm/s.f. for 10 mins....in my case 480 gallons
2) Recharge: 5# of salt per c.f. of resin, in my case I have 40 c.f. of resin in each vessel, therefore requiring 200# of salt per vessel. Brine is assumed to be 2.5# of salt per gallon of brine, so it will pull 80 gallons of brine into a flow of 1/2 gpm per c.f. This gives 900 gallons of water containing 80 gallons of brine.
3) Rinse: 10 min at 4 gpm/sf...in my case 480 gallons per vessel.
The total flow to the waste stream is then 1860 gallons containing 200# of salt, for each vessel. In my case I had two vessels so I used a SAY value of 4,000 gallons and 500# of salt.
So, we have:
500/(4,000 * 8.34) = 0.015 (15 parts per thousand) as a slug flow to the waste stream. In reality one might argue that this flow mixed with the other wastewater already in the wastestream might be under the 8 parts threshold. However, in my case, that wasn't an agreeable approach so we dosed it into the sewer over a day.
The receiving WWTP has an average flow of 60,000gpd. As a general check, 500/(60,000 * 8.34) = 0.001 (1 part per thousand).
What's frustrating is that when you look at the big picture, the WWTP is not going to remove the salt, so it doesn't really make any sense to me to put the salt through the plant...the salt is ultimately going to end up in the river....but I just do what the regulators tell me.
Hope this helps.