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New Sac manual ch 4
Test questions- multiple choice
| Question | Answer |
|---|---|
| What is the purpose of presedimentation facilities? | To reduce the solids removal load at the water treatment plant. |
| What size particles can be removed from water by sedimentation? | Greater than 10 microns. |
| What property of alum attracts negatively charged particles? | Positive charge. |
| What happens to the settling rate (settling velocity) of particles in water when the water temperature drops? | Decreases |
| What is the largest portion of the sedimentation basin? | Settling zone |
| Calculate the theoretical detention time for a rectangular sedimentation basin in hours. The basin is 80 feet long, 30 wide and 10 deep treating a flow of 1.8 MGD. | 2.4 hrs. 80x30x10x7.48 gal/ft3 = 179,520gal/ft3. 179,520 gal/ft3 x 24 hrs = 4,308,480gal/ft3/24hrs. Divided by 1,800,000 MGD = 2.39 hrs. |
| What is a major means by which operators can control water treatment processes? | Adjusting chemicals and chemical feed rates. |
| Estimate the surface loading rate in gallons per minute per square foot for a rectangular sedimentation basin 20 ft wide by 40 ft long when flow is 0.5 MGD | 0.43 gpm/ft2. 0.5 MGD divided by 1440 min/day = 347 gpm divided 40x20 = 800ft2. 347 divided by 800 = 0.43 gpm/ft2 |
| Determine the mean flow velocity in ft/min) for a rectangular sed basin with a flow of 2.0 MGD. The basin is 75 ft long, 25 wide and 14 deep. | 0.53 ft/min 2.0 MGD div by 1440 min/day = 1389 gpm. multiply by 1 gal over 7.48 gal/ft3 (or divide by 7.48) = 185.68. 185.68 over (25 ft wide x 14 ft deep) = 0.53 ft/min |
| Determine the weir loading rate in gpm/ft of weir for a rectangular sed basin basin with flow rate of 2.0 MGD. Four effluent launders 10.5 ft long with v-notch weirs on both sides of the launder extend into basin from outlet end. | 16.5 gpm/ft. 2MGD/1440 min per day = 1388 gpm. 10.5 ft per weir x 2 (per basin) = 21 ft. 21ft x 4 weirs = 84 ft. 1388 gpm/84 ft = 16.5 gpm/ft. |
| --- combine the caogulation, flocculation and sedimentation processes into a single basin. | The solids-contact process units |
| Sludge produced by a solids-contact clarification unit is recycled through the process to act as a ----- | coagulant aid |
| Changes in which process variables cause instability in solids-contact units? | Flow, temperature and turbidity. |
| What does the volume over volume test result tell an operator about the solids-contact unit? | Percentage of slurry. |
| If raw water at treatment plant needs a lime does of 10.5 mg/L, determine setting time on lime feeder in lbs/day. Flow is 1.5 MGD. | 131 lbs/day 10.5 mg/L x 1.5 MGD x 8.34 lbs/gal = 131 lbs/day |
| What is the primary factor in determining the frequency of sludge removal? | Rate of sludge buildup. |
| Low turbidity source waters may not require ---- | sedimentation |
| Which water quality indicators should be monitored in the normal operation of the sedimentation process? | Temperature and turbidity. |
| In solids-contact clarifiers, what should an operator do if the sludge blanket is of normal density but very close to the surface? | Waste more sludge. |
| What does frequent clogging of the sludge discharge line indicate? | Sludge concentration is too high. |
| How can operators measure turbidity levels at the sedimentation basin inlet and outlet to get a rough idea of process removal efficiency? | Grab samples. |
| What is the most common reason to shut down a sedimentation basin? | Annual maintenance and cleaning. |
| Which task should be performed immediately following dewatering of a sedimentation basin? | Grease and lubricate previously submerged mechanical moving parts. |
| Process water samples must be --- of actual conditions in the treatment plant. | representative. |
| How can operators determine if sludge pumping lines are clogged? | Check pump's suction and discharge pressure. |