To accommodate the possibility of a future petition for disinfection credits, the ozone system vendor built in appropriate time with ozone in the contact tank to allow for disinfection. To also counter taste and odor sources of algae, Geosmin, and methylisoborneol (MIB), they recommended ozone concentrations of 1–3 ppm there.
Click here to enlarge image“They also built in appropriate contact time for the ozone to allow for disinfection, and established the system as redundant to greatly enhance its reliability, as well as allow for flexible and economical operation. It’s much easier to control something at 75% of capacity than at 40%, including assuring you’re not overfeeding ozone.”
“The Illinois Environmental Protection Agency (IEPA) has a history of being conservative with changes to regulations,” Roth noted, “which is not a bad thing in a state that has a tremendous variety of treatment systems. They have to be careful how they craft regulations in order to cover different types of situations. Charleston may do a very good job, but it’s hard to generalize for all cases. In time, the disinfection issue will work itself out, and when it does, this city will be prepared.”
The 4.5 mgd, cone–style SWTP has a lime softening process that uses an upflow clarifier. It came on line in April 2005, and has run at an average of 1.9 mgd, with peak at 2.7 mgd and low at 1.2 mgd. It replaced a plant built in 1964 that could no longer meet a change in the IEPA turbidity requirement from 0.5 NTU to 0.3 NTU, 95% of the time.
“That was a source of major complaints for 25 years,” Bosler said. “Our 350–acre reservoir has an average depth of only 8 feet, and major summertime algae blooms resulted in taste and odor degradation. To fix the problem over the years with the old plant, we tried powdered activated carbon, potassium permanganate, and chlorine dioxide, but nothing would do the job 100% of the time. We put ozone treatment out to bid as part of the new plant, and finally got the reliable solution we needed.”
With the new plant, a pump station at the reservoir moves raw water to the head tank, where a cationic polymer is injected with liquid alum. Lime is added in two, 36 ft. diameter cones, before movement by gravity flow to the carbonation tank and ozone contact tank. The ozone–treated flow is pumped to four, 18 ft. decelerating flow filters, each of which has a 5 ft. bed of granular activated carbon and a 2 ft. bed of sand.
Fluoride and sodium hypochlorite are injected before entry to the ribbon–flow, 400,000 gallon clearwell. At the high service pumps, a final dose of sodium hypochlorite is added with ammonia before the flow is pumped to the distribution system.
“The ozone system vendor we selected had by far the superior presentation, and they were very knowledgeable and helpful throughout the pilot study and full–scale project,” Bosler said. “The only previous ozone installation we knew of in Illinois had been placed at the raw water pumping station. Ours was the first in the state to be put in the center of the treatment train. There’s no need to kill stuff your normal process is going to remove.”
To counter taste and odor sources of algae, Geosmin, and methylisoborneol (MIB), MEPPI recommended ozone concentrations of 1–3 ppm in the contact tank. Previously in the train, the water receives 4 ppm of cationic polymer, 25 ppm of alum, 150 ppm of lime, and 3 ppm of CO2. Following the ozone contact tank, it is treated with 1 ppm fluoride, a first chlorine dose of 1.5 ppm, and a final chlorine dose of 3 ppm, with 2 ppm of ammonia.
The ozone system includes a 1500 gallon liquid oxygen storage tank, a vaporizer to produce gaseous oxygen, and two 100–lb./day, 10% ozone–by–weight generators. An ozone pump injector skid introduces the ozone into the contact tank. The system occupies a footprint within the plant’s main building of 37 ft. x 26 ft., plus a separate building outside on a footprint of 20 ft. x 30 ft.
From the contact tank, unused ozone is brought back for reduction to oxygen and release to the atmosphere. The system also includes two 25–gal./min. water chiller units, and a nitrogen–boost skid to supply a small amount of nitrogen during the ozone generation process.