Filtration
Water Treatment Plant Operation
Volume 1
Sixth Edition
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A buildup of head loss (pressure drop) across the filter media until it reaches some predetermined design limit
A crack or break in a filter bed allowing the passage of floc or particulate matter through a filter
A mass of solid particles that is made to flow like a liquid by injection of water
A process of reversing the flow of the water through the filter media to remove the entrapped solids
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The removal of iron and manganese from the water being treated
The removal of particulate impurities and floc from the water being treated
The removal of pathogens from the water being treated
The removal of tastes and odors from the water being treated
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Because of high quality source water
Because of low demands for water
Because of reliability and minimum operation and maintenance requirements
Because of the availability of slow sand
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A measure of the amount of water that can be processed through an individual filter module in a given time period
A measure of the flow of water through a filter
A measure of the head loss through a filter
A measure of the velocity of water flowing down through a filter
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Checking and adjusting process equipment (changing chemical feed rates)
Evaluating filter media condition (media loss, mudballs, cracking)
Evaluating water quality conditions (turbidity) and making appropriate process changes
Monitoring process performance
Visually inspecting facilities
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A device which calibrates turbidimeters
A device which counts and measures the size of individual particles in water
A device which identifies the origin or source of particles
A device which measures turbidity
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To allow filter boils to develop uniformly
To ensure the loss of light of small-diameter filter media
To permit purging (removing) of any entrapped air from the filter media, and also to provide uniform expansion of the filter bed
To prevent damage from water hammer
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The gathering of a gas, liquid, or dissolved substance on the surface or interface zone of another material
The sedimentation of particulates in very small spaces in a rock or granular material
The straining of particles through the pores in a filter
The taking in or soaking up of one substance into the body of another by molecular or chemical action
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In order to cleanse the filtered water before disinfection (chlorination)
In order to encourage mudball formation for subsequent removal
In order to produce optimum cleaning of the filter media during backwashing and to prevent mudballs
In order to reduce the volume of backwash water required
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An adequate supply of the filter aid chemical may not be readily available
Extra safety precautions must be taken with higher filter aid chemical feed rates
Overdosing can cause a violation of the MCL
Overdosing can cause sealing of a filter media resulting in drastically shortened filter runs
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Checking the filter media condition
Checking the filtration process and backwash equipment condition
Inspecting the facilities
Making visual observations of the backwash operation
Operating the filters and backwash
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By adjusting backwash flow rates
By adjusting backwash surface wash duration
By adjusting backwash surface wash flow rates
By adjusting the duration of the backwash cycle
By adjusting the time sequence of the backwash cycle
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Immediately contact the consumer (stakeholders)
Immediately enroll in an appropriate training course
Immediately notify the news media
Immediately review the performance of the filtration process
Immediately Immediately review the pretreatment process (coagulation, flocculation, and sedimentation)
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Each filter effluent control valve is connected to a flow-meter and, as the filter run continues and the media begins to clog, the control valve slowly opens to maintain a constant flow of water through the filter
The flow rate varies with head loss and each filter operates at the same, but variable, water surface level
The flow to each filter influent is split or divided to each weir and equal flow is automatically distributed to each filter
The influent flow to each filter is divided by a weir and the water surface level in each filter varies according to headloss, but the flow rate remains constant for each filter
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When applications of the floc build up on the material previously deposited on the media surface
When the floc buildup causes taste and odors
When the floc buildup on the filter media degrades
When the period of floc buildup reaches excessive headloss
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Because clogging or breakthrough will increase filter maintenance requirements
Because clogging or breakthrough will require additional space for sludge disposal
Because clogging or breakthrough will require more backwash water
Because when breakthrough occurs, there will be an increase in filtered water turbidity
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Effluent turbidity levels
Length of the filtration cycle
Unit Filter Run Volume (UFRV) technigue
Volume of backwash water per cycle
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At filtration rates when filtered water has high turbidity levels
At filtration rates when mudballs tend to form during backwash
At high filtration rates when iron and alum floc will shear in the pores of the filter and short filter runs will result because of turbidity breakthrough
At high filtration rates when there is insufficient water in the backwash water tank
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5,000 gal/sq ft
5,600 gal/sq ft
6,000 gal/sq ft
6,200 gal/sq ft
6,400 gal/sq ft
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The gathering of a gas, liquid, or dissolved substance on the surface or interface zone of another material.
The sedimentation of particulates in very small spaces in a rock or granulated material
The straining of particles through the pores in a filter
The taking in or soaking up of one substance into the body of another by molecular or chemical action
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1.11%
1.22%
1.30%
1.39%
1.56%
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Does not react with substances in the water (is inert and easy to clean up)
Free of impurities
Good hydraulic characteristics (is permeable)
Hard and durable
Insoluble in water
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Clumps of bacteria and particulate impurities that have come together and formed a cluster
Very small, finely divided solids (particles that do not dissolve) that remain dispersed in a liquid for a long time due to their small size and electrical charge
Very small open spaces in a rock or granular material
Very small solids suspend in water which can vary widely in size, shape, density, and electrical charge
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1.3 psi
1.5 psi
1.7 psi
1.9 psi
2.2 psi
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1.9 GPM/sq ft
2.1 GPM/sq ft
2.3 GPM/sq ft
2.5 GPM/sq ft
2.7 GPM/sq ft
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624 lbs/sq ft
749 lbs/sq ft
998 lbs/sq ft
1,122 lbs/sq ft
1,248 lbs/sq ft
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Keep the filters clean by backwashing
Minimize the head loss through the filters
Perform the jar tests on a regular basis
Select an effluent turbidity goal (level) and stay below the target value
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Handling and delivery
Preservation and storage
Retrieval and delivery
Storage and retrieval
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112,300 lbs
122,000 lbs
131,000 lbs
149,800 lbs
168,500 lbs
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Electrical equipment
Mechanical equipment
Open-surface filters
Pathogenic organisms
Valve and pump vaults, sumps, and filter galleries
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False
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Effectiveness of the pretreatment process in conditioning the suspended solids for removal by sedimentation and filtration
Filter operation
Quality of the water being treated
Recordkeeping program
Weather conditions
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Excessive noise
Excessive vibration
Leakage (water, lubricants)
Overheating
Volute flow
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