Clarifier Maintenance Procedures The Water and Wastewater Equipment Company inclined plate clarifier is designed for ease of maintenance and when operated properly will require minimal control and operator time. Periodic maintenance of the inclined plate clarifier should be done to assure proper operation. The following steps can aid in the inclined plate clarifier operation and control:
Trouble Shooting
Principle Of Operation The wastewater being introduced to the inclined plate clarifier must be:
The water enters the inclined plate clarifier by gravity from the flocculation tank through disperse pipe located above the cone to uniformly disperse the solution in the inclined plate clarifier. The ports in the disperser pipe are installed with the ports on the bottom of the pipe forcing discharge of the solution downward. Upon entering the inclined plate clarifier, the velocity of the solution is reduced sufficiently to allow for the gravity separation of the metal hydroxides from the water. The metal hydroxides move downward and the clear water moves upward being displaced by the new solution entering the inclined plate clarifier. Clear water overflows the weir for discharge or further filtration. The linear length of the weir is designed to minimize the water head over the weir. This also reduces the velocity of the water and restricts the capillary action of the decanting solution that might pull light particles of floc along with the water. “Snowing” in the clear water may be attributed to improper dosages of Polyelectrolyte, improper pH range or insufficient height of the sludge blanket. Air bubbles entrapped in the water along with the floc may also be attributed to this condition. It is Important that the height of the sludge blanket be maintained over the disperser when drawing off sludge for dewatering. It is recommended that this height be maintained to approximately 10 to 12 inches. Do not allow the sludge blanket to rise too close to the decant weir. Capillary action of the decanting water may track some of the sludge over the weir. Sludge draw-off for dewatering may be done continually or periodically to maintain the sludge blanket maximum and minimum levels discussed. It is important that the sludge be removed slowly to eliminate a rat-holing effect through the sedimentation tank, thereby removing mostly water and only small amounts of sludge. This condition also restricts the downward movement of sludge along the sides of the cone. Natural compaction of the sludge in a gelatinous condition is harder to move. This condition is evident when a coning condition is detected in the center of the sludge bed. This condition requires air lancing and agitation of the sludge bed. To correct this situation it is necessary to take the inclined plate clarifier out of service temporarily.
Should mistreated water be detected in the inclined plate clarifier and sludge bed becomes contaminated, it would become necessary to batch treat the inclined plate clarifier. Use of the air lance technique described may be used for mixing the treatment chemicals added to the inclined plate clarifier. |
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