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Water Treatment Question

front 1

What are the general water quality characteristics of surface water supplies

back 1

low calcium and magnesium content (soft water), turbidity, suspended solids, some color, and microbial contamination.

front 2

What are the general water quality characteristics of groundwater supplies

back 2

contains dissolved solids, dissolved gases, high hardness, free of suspended solids, and free of microbial contamination.

front 3

What are the general water quality characteristics of groundwater supplies

back 3

contains dissolved solids, dissolved gases, high hardness, free of suspended solids, and free of microbial contamination.

front 4

How can the sustained yield of an aquifer be exceeded

back 4

if a well draws out more water than is replaced, causing subsidence (settling of the ground as water is removed).

front 5

List the three basic water rights

back 5

Appropriative, prescriptive, and riparian.

front 6

What is the purpose of a sanitary survey

back 6

determine how much water is available and if it is safe to drink/use.

front 7

When conducting a sanitary survey, what protective measures should be investigated regarding use of the watershed

back 7

control fishing, boating, landing of airplanes, swimming, wading, ice cutting, and permitting animals on shoreline areas.

front 8

List the common physical characteristics of water

back 8

water color, turbidity, temperature, taste, and odor.

front 9

What causes turbidity in water

back 9

the presence of suspended material in water.

front 10

Chemical analysis of a domestic water supply measures what three general types of chemical concentrations

back 10

inorganic chemicals, organic chemicals, and general mineral constituents.

front 11

Why are coliform bacteria used to measure the bacteriological quality of water

back 11

they are always present in fecal wastes and outnumber other pathogenic organisms.

front 12

What tastes/odors are caused by algae

back 12

fishy, aromatic, grassy, septic, musty, and earthy.

front 13

Increased organic loadings from algal blooms can cause what kinds of water quality problems

back 13

increased color and increase in chlorine demand, leading to increased costs.

front 14

What is the influence of algal blooms on dissolved oxygen

back 14

DO increases as algae produces it via photosynthesis.

front 15

What problems are caused by anaerobic conditions in reservoirs

back 15

hydrogen sulfide may be produced by anaerobic bacteria as they consume organic matter.

front 16

What is the primary purpose of reaeration-destratification programs in domestic water supply reservoirs

back 16

eliminate, control, or minimize negative effects on domestic water quality that occur during periods of thermal stratification and DO depletion.

front 17

How can water quality be improved by reaeration destratification

back 17

add DO to zones that become anaerobic during thermal stratification.

front 18

List two basic methods of maintaining/increasing DO in reservoirs when thermal stratification occurs

back 18

destratification through aeration, and adding DO to the hypolimnion (hypolimnetic aeration/oxygenation).

front 19

What are nonsettleable solids

back 19

also called colloidal matter, bacteria, clay/silt that does not
easily settle and must be coagulated.

front 20

What happens in the coagulation/flocculation processes

back 20

particulates clump together in coagulation with chemicals and clump further in the flocculation process.

front 21

What is the primary purpose of flash mixing

back 21

mix chemicals with raw water containing
particulates that do not easily settle/filter out.

front 22

Why are both primary coagulant and coagulant aids used in coagulation

back 22

primary coagulants remove the electrical charge while aids add density and toughness to prevent floc breakdown.

front 23

List four methods of mixing coagulant chemicals into the plant flow

back 23

hydraulic mixing using flow energy in the system, mechanical mixing, diffusers and grid systems, and pumped blenders

front 24

Describe the results of inefficient mixing during flocculation

back 24

ineffective collisions and poor flocculation of particulates; may tear the floc apart.

front 25

What is the minimum recommended detention time for flocculation

back 25

5-20 minutes for direct filtration and 30 minutes for conventional filtration.

front 26

What is the advantage of vertical flocculators over horizontal flocculators

back 26

they require less maintenance as they eliminate submerged bearings and packings.

front 27

Why are the compartments in flocculation basins separated by baffles

back 27

prevent short circuiting of water; water following a path may flow too fast, not enough time to settle/react.

front 28

Why is coagulation-flocculation treatment important to other treatment processes

back 28

for efficacy purposes, reduce THM production, reduce pathogens.

front 29

What is the most important consideration in coagulation-flocculation process control

back 29

selection of the proper type and amount of coagulant chemicals to be used.

front 30

Which processes remove suspended solids after the CF process

back 30

sedimentation and filtration.

front 31

List the typical functions performed by an operator in the normal operation of the CF process

back 31

monitor process performance, evaluate water quality conditions, check and adjust process controls and equipment, and visually inspect facilities.

front 32

How is the effectiveness of solids removal process normally monitored

back 32

visual observations and laboratory testing.

front 33

Which lab tests would you use to monitor the CF process

back 33

water quality indicators used to evaluate coagulant dosage and process performance include turbidity, temperature, alkalinity, pH, color, and chlorine demand.

front 34

What would you look for when visually observing the performance of a CF process

back 34

leaves, twigs, odors, and organic matter.

front 35

Why do many operators prepare flow v. detention time curves for basins in their plans

back 35

allows for easy selection of stirring times when performing jar tests.

front 36

What is the goal in setting up a jar test

back 36

see how chemicals chemical doses, mixing times, and other parameters will affect the plant’s performance on a smaller scale.

front 37

Why should jar test samples have the same temperature as water in the plant

back 37

temperature can affect floc formation; running at different temperatures can provide information on how temperature affects the process.

front 38

Why are anionic and nonionic polymers used as coagulant aids often prepared as dilute solutions

back 38

dilution prevents a viscous material from being formed.

front 39

List the four zones into which a typical sedimentation basin can be divided

back 39

Inlet zone, settling zone, sludge zone, outlet zone.

front 40

What are launders

back 40

sedimentation basin and discharge channels consisting of overflow weir plates and conveying troughs.

front 41

Three possible shapes for sedimentation basins

back 41

rectangular, circular and square, double deck.

front 42

List advantages/disadvantages of double deck sedimentation basins

back 42

surface area is doubled, but are more costly and if an issue arises in either deck, the entire operation must be shut down.

front 43

Why are rectangular basins preferred over circular ones

back 43

less likely to short circuit and particle removal issues.

front 44

During operation of a solids-contact unit, what items should be of particular concern to the operator

back 44

a uniform sludge blanket is formed and maintained throughout the soldis removal process.

front 45

How would you calculate the detention time for a sedimentation basin

back 45

dividing the volume of the basin by the flow going into the basin.

front 46

What problems are caused by reduced effective water depth from excessive sludge buildup

back 46

high flow velocity, sludge scouring, and degradation of process efficiency.

front 47

Name two kinds of launders used in basin outlets

back 47

V-notch weirs, and orifices in pipes.

front 48

List two advantages of solids-contact units

back 48

capital and maintenance costs, and volume adjustment of sludge blankets.

front 49

How can the level of the sludge blanket be determined in solids-contact units

back 49

placing sampling taps at various depths along the wall of the solids-contact reactor.

front 50

What should be done when a rapid change in turbidity is expected

back 50

early application of an increased chemical dose.

front 51

How is the proper chemical dose selected when operating a solids-contact unit

back 51

jar testing.

front 52

List the devices that may be used to provide recirculation in a solids-contact unit

back 52

impeller, turbine, pumping unit, or air injection.

front 53

How is the percentage of slurry present in the reaction zone determined

back 53

performing a volume over volume test (settled slurry/total sample volume)

front 54

Under what circumstances are sedimentation basins needed to treat water

back 54

remove suspended solids and reduce load on the filters

front 55

What is the difference between normal operations and abnormal operations

back 55

normal operations are within operating ranges while abnormal operations are unusual or difficult to handle operations.

front 56

The actual performance of sedimentation basins depends on what two major factors

back 56

turbidity of the water and temperature of the water.

front 57

How can an operator determine if sludge lines are free flowing

back 57

if sight glasses are incorporated in the sludge discharge piping.

front 58

What should be changed if the sludge line plugs frequently

back 58

frequency of sludge removal must be increased.

front 59

How often should visual observations of sedimentation process performance be conducted

back 59

frequently/day by day.

front 60

In the routine operation of the sedimentation process, what types of records should be maintained

back 60

influent/effluent turbidity and influent temperature, process production inventory, and process equipment performance.

front 61

What water quality indicator is used as a rough measure of sedimentation basin process removal efficiency

back 61

measurement of turbidity levels.

front 62

What problems can be created by a sudden increase in settled water turbidity

back 62

filtration error.

front 63

What actions might an operator take if the sludge is rising or floating in a sedimentation basin

back 63

observe floc settling characteristics (dispersion, size, settling rate), evaluate process performance, perform jar tests, make changes and verify response to process changes.

front 64

Why should photographs be taken during shutdown and startup procedures

back 64

provide a visual record of events that may be difficult to illustrate when a basin is full of water.

front 65

List steps in the shutdown process for a sedimentation basin

back 65

stop flow to basin, install isolation gates, turn off sample pumps and sludge removal, lock out and tag electric switches and equipment, dewater basin, grease and lubricate all gears, sprockets, mechanical parts that were submerged to avoid freezing/breakage.

front 66

How frequently should turbidity be monitored

back 66

several times per shift.

front 67

How are sedimentation process water samples obtained for analysis

back 67

immediately taken in clean plastic/glass containers and without contaminants.

front 68

What items should an operator look for after a sludge pump has been started

back 68

check for noises, vibration, temperature, leaks, suction and discharge pressures.

front 69

List typical functions performed as part of a sedimentation process preventative maintenance program

back 69

keep motors free of dirt and moisture, ensure good ventilation, check pumps and motors for leaks, noise, vibration, etc, maintain lubrication, inspect alignment of shafts and couplings, check bearings, check proper valve operation, check free flow of sludge in sludge removal collection and discharge systems.

front 70

What types of safety hazards are associated with sludge removal equipment

back 70

electrical, mechanical, open surface water, valve and pump vaults, sumps.

front 71

What is the difference between conventional and direct filtration

back 71

conventional filtration involves coagulation, flocculation, and sedimentation, while direct omits sedimentation and flocculation is reduced/omitted as well.

front 72

List the particle removal mechanisms involved in the filtration process

back 72

sedimentation on media, adsorption, biological action, absorption, and straining.

front 73

List the four classes of filters

back 73

gravity filtration, pressure filtration, diatomaceous earth, slow
sand filtration.

front 74

Define garnet

back 74

reddish glassy mineral sands made of silicates (calcium, magnesium, iron, and manganese)

front 75

What material is used for precoat and body feed operation

back 75

diatomaceous earth.

front 76

What material is most often used to support granular filter materials

back 76

gravel.

front 77

What units are commonly used to express filtration rate

back 77

gal/min/ft^2 or L/sec/m^2

front 78

What is the major operational difference between sand and dual media filters

back 78

sand filters have light fine grains on the top to stop floc, dual media filters have larger diameter grains in the top layer to stop larger particulates.

front 79

What two main factors influence the time period before a filter becomes clogged

back 79

amount of suspended solids in the water, and filtration rate.

front 80

Under what conditions is the filtration process stopped and the filter taken out of service for cleaning/backwashing

back 80

filter clogged, breakthrough occurs, or sufficient time has passed.

front 81

List four types of surface wash systems for filters

back 81

Baylis, fixed-grid, rotary, and air scour.

front 82

What aspects of the filtration process are controlled by the filter control system

back 82

flow rates through the filter by maintaining an adequate head above the media surface.

front 83

What is the primary purpose of using activated carbon as filter media

back 83

remove tastes and odors.

front 84

What is inline filtration

back 84

addition of filter aids to the filter inlet pipe.

front 85

What water quality factors affect the floc formation during inline filtration

back 85

variable turbidity and bacterial levels.

front 86

When is direct filtration used

back 86

when source water is low in turbidity, color, plankton, and coliform organisms.

front 87

What factors must an operator measure to control the performance of the filtration process on a day to day basis

back 87

turbidity (influent and effluent), and filter performance.

front 88

What is the most important water quality indicator used to monitor the filtration process

back 88

effluent water turbidity.

front 89

How can filter effluent turbidity be measured on a continuous basis

back 89

by an in-process turbidity meter.

front 90

List some of the typical functions performed by operators in the normal operation of the filtration process

back 90

monitor process performance, evualte water quality conditions and make appropriate changes, check and adjust process equipment, backwash filters, evaluate filter media condition, visually inspect facilities.

front 91

What could cause a sudden increase in head loss through a filter

back 91

lack of depth penetration.

front 92

How would you change the operation of a filter if there was a sudden increase in head loss through the filter

back 92

adjust filter aid chemical feed rate or reduce filtration rate.

front 93

What is meant by bumping a filter

back 93

opening backwash valve during a filter run to dislodge trapped solids and increase filter run length.

front 94

List the type of process calculations an operator is expected to perform

back 94

filter operation, backwashing, water production, and percent of water production used to backwash filters.

front 95

How are filter backwash rates usually given

back 95

gal/min/ft^2 or L/sec/m^2 of surface area.

front 96

Calculate the percent of water filtered used for backwashing if a filtration plant uses 0.12M gallons for backwashing during a period when a total of 5M gallons of water was filtered

back 96

2.4

front 97

What types of records should be kept when operating a filtration process

back 97

water quality, operation, water production, percent of water production for backwashing, and equipment performance.

front 98

How would you identify an upset or failure in the filtration/pretreatment process

back 98

abrupt changes in turbidity, pH, alkalinity, TON, temperature, chloring demand/residual, or color.

front 99

List indicators of abnormal filtration process conditions

back 99

mudballs in filters, media cracking/shrinkage, media boils during backwash, excessive media loss or disturbance, shorter filter runs, uncleanable filters, algae on walls and media.

front 100

How could you make a quick determination of filtration removal efficiency

back 100

changes of source water quality, pH, and alkalinity.

front 101

What problems may be encountered during backwash

back 101

mudball formation, filter cracks/shrinkage.

front 102

How does a filter become air bound

back 102

release of dissolved air in saturated cold water due to a decrease in pressure.

front 103

Under what conditions may clean filters be put back into service

back 103

when a dirty filter is removed, to decrease filtration rates, or increase production for increased demand.

front 104

When are filters routinely taken off for backwashing

back 104

when media is clogged, turbidity breakthrough occurs, or water demand is reduced.

front 105

Why should the surface wash system be activated just before the backwash cycle starts

back 105

aid in breakdown and removal of solids, prevent mudball development.

front 106

What should be done if a filter will be out of service for a prolonged period

back 106

drain water to avoid algal growth.

front 107

List types of equipment used in the filtration process

back 107

filter control valves, backwash/surface water pumps, flowmeters and level/pressure gauges, water quality monitors (turbidity meter), process monitors for head loss and water levels, mechanical and electrical filter control systems

front 108

What should be done before starting a piece of mechanical equipment such as a backwash pump

back 108

be sure it has been serviced and operational status is positively known.

front 109

What safety hazards may be encountered when working around mechanical equipment

back 109

rotating equipment, energized valves, pumps and other pieces of equipment, chemical spills

front 110

What is the SWTR definition of surface water

back 110

all water open to the atmosphere and subject to surface runoff.

front 111

What is the SWTR definition of surface water

back 111

all water open to the atmosphere and subject to surface runoff.

front 112

Particle counts can be used as a substitute for indicating the potential removal of what two microorganisms that are a threat when found in drinking water

back 112

giardia and cryptosporidium cysts.

front 113

Particle counters can be used to enhance the performance of which water treatment process

back 113

N/A

front 114

What is the difference between turbidity meter and particle counter measurements

back 114

N/A

front 115

What two factors influence the effectiveness of disinfection on microorganisms

back 115

reactions with organics and reducing agents.

front 116

List chemical agents that have been used for disinfection other than chlorine

back 116

bromine, iodine, ozone, bases.

front 117

What is a major limitation of the use of ozone

back 117

solubility.

front 118

How is chlorine dosage determined

back 118

add chlorine needed for chlorine demand and chlorine residual.

front 119

How is chlorine demand determined

back 119

chlorine does not react any longer with organic/inorganic materials.

front 120

List two inorganic reducing chemicals with which chlorine reacts rapidly

back 120

hydrogen sulfide and ammonia.

front 121

How do chlorine gas and hypochlorite influence pH

back 121

chlorine gas lowers pH by forming HCl, hypochlorite raises pH forming hydroxyl ions.

front 122

How does pH influence the relationship between HCl and OCl- - HCl favors formation of hypochlorus acid, OCl- is formed from HOCl at pH 8.5 or higher.

back 122

N/A

front 123

What is breakpoint chlorination

back 123

adding chlorine until demand has been satisfied.

front 124

An operator’s decision to use chloramines depends on what factors

back 124

quality of raw water, plant regulations, operational practices, and distribution system practices.

front 125

What are the three primary methods by which chloramines are produced

back 125

preammoniation followed by later chlorination, concurrent ammonia and chlorine addition, post chlorination/ammoniation.

front 126

Why is the applied chlorine to ammonia nitrogen ratio usually greater than the actual chlorine to nitrogen ratio leaving the plant

back 126

chlorine demand will reduce amount of chlorine available from combined residual.

front 127

Incomplete nitrification causes the production of nitrite, producing what problems in water disinfection

back 127

rapid reduction of free chlorine and interferes with measuring free chlorine,
leading to loss of chlorine/ammonia, increase in count of heterotrophic plate count bacteria.

front 128

What actions should an operator take when there is a sudden absence of chlorine residual in the distribution system

back 128

Retesting for chlorine residual, then checking chlorination equipment,
and finally searching for a contamination source that could cause an increase in the chlorine demand.

front 129

How does the length of chlorine contact time affect the disinfection process

back 129

With good initial mixing the longer the contact time the better the disinfection.

front 130

How is the efficiency of a disinfectant measured

back 130

Time in minutes of disinfectant’s contact in the water and concentration of the disinfectant residual.

front 131

List the two most common points of chlorination in a water treatment plant

back 131

Pre chlorination and post chlorination.

front 132

Under what conditions should waters not be pre chlorinated

back 132

Raw water containing organic precursor compounds and tasting orders when phenolic compounds are present.

front 133

What are the benefits of pre chlorination

back 133

Control of algae and slime growths, control of mud-ball formation, improved coagulation, reduction of tastes and odors, increased chlorine contact time, and increased safety factor in disinfection of heavily contaminated waters.

front 134

List the major parts of a typical hypo chlorinator system

back 134

solution, pump/ejector, treated wastewater from plant.

front 135

What are the two most common methods of feeding hypochlorites to the water being disinfected

back 135

The hypochlorites solution may be pumped directly into the water or the
hypochlorite solution is pumped through an ejector.

front 136

How is the rate of gas flow in a chlorinator measured

back 136

Through use of a rotameter.

front 137

What is the primary advantage of vacuum system chlorinators

back 137

Safety.

front 138

What type of container is commonly used to store hypochlorite

back 138

Plastic containers.

front 139

How large a supply of hypochlorite should be available

back 139

One week supply

front 140

What is the purpose of the fusible plug

back 140

Prevent buildup of excessive pressures and the
possibility of rupture due to a fire or high surrounding temperatures.

front 141

What is removed by the upper and lower valves of ton chlorine tanks

back 141

Upper valve releases chlorine gas, lower valve releases liquid chlorine.

front 142

When are mouthbit chemical cartridge respirators used

back 142

Only for escape.

front 143

How can copper tubing be prevented from getting kinks or dirt inside the tubing

back 143

Use of a sling to hold the tubing when disconnecting it from an empty container to prevent the tube from flopping around.

front 144

Why are one ton tanks placed on their sides with the valves in a vertical position

back 144

So that either chlorine gas or liquid chlorine may be removed.

front 145

What would you do before attempting to start any chlorination system

back 145

Read the manufacturer’s literature and your plant’s operation and maintenance instructions.

front 146

What should be the chlorine residual in the most remote part of the distribution system

back 146

0.2 milligrams per liter.

front 147

Why should a hypo chlorite feed pump be operated in the upper end of its range (at 6 or 7 in a range of 0 to 10)

back 147

So that the strokes or pulses from the pump will be close together. This way, the chlorine will be fed continuously to the water being treated.

front 148

When starting a gas chlorinator, how is the system checked for chlorine gas leaks

back 148

With a chlorine leak detector.

front 149

List the steps to follow when shutting down a chlorinator for a long time period

back 149

Have safety equipment available in the event of a chlorine leak, close chlorine container gas outlet valve, Allow chlorine gas to completely evacuate the system through the injector. Chlorine gas pressure gauges will fall to 0PSI on the manifold and the chlorinator. Close chlorinator gas discharge valve. The chlorinator may remain in this condition indefinitely and is ready to be plugged back into surface by reopening the chlorinator discharge valve and the chlorine gas container valve. Turn off the chlorinator power switch, lock out, and tag. Secure the chlorinator
gas manifold and chlorinator valve in closed position.

front 150

Normal operation of a chlorinator includes daily inspection of what facilities or areas

back 150

Container storage areas.

front 151

What is the purpose of evaporators

back 151

Evaporators are used to convert liquid chlorine to gaseous chlorine for use by gas chlorinators.

front 152

What abnormal conditions could be encountered when operating an evaporator

back 152

The evaporator water level is low. Low water temperature in the evaporator, no chlorine gas flow to the chlorinator.

front 153

What are possible chlorinator abnormal conditions

back 153

Chlorine leak in the chlorinator, gas pressure is too low less than 20PSI, injector vacuum is too low, low chlorine residual.

front 154

How can you determine if the chlorine residual analyzer is working properly

back 154

Determine the actual chlorine residual and compare it with the residual reading from the chlorine analyzer.

front 155

What is the suggested free chlorine residual for treated water

back 155

0.5 to 1.5 mg/L

front 156

What is the suggested free chlorine residual for the farthest points in the distribution system

back 156

0.2 mg/L

front 157

How would you determine if you were chlorinating at the breakpoint –

back 157

Increase the chlorine dose rate.

front 158

If chlorine is escaping from a cylinder, what would you do

back 158

turn the container so that the leaking side is on top

front 159

How can chlorine leaks around valve stems be stopped

back 159

By closing the valve or tightening the packing gland nut.

front 160

How can chlorine leaks at the valve discharge outlet be stopped

back 160

Replacing the gaskets or adapter connection.

front 161

Why should a chlorinators be located in a separate room

back 161

prevent Chlorine gas leaks from damaging equipment and harming personnel.

front 162

Why is adequate ventilation important in a chlorinator room

back 162

Remove any leaking chlorine gas that would be hazardous to personnel and damaging to equipment.

front 163

How can chlorination rates be checked against the chlorinator setting

back 163

measuring and controlling chlorine dosage.

front 164

When and how often should the weights of chlorine containers be recorded

back 164

At the same time every day.

front 165

What additional equipment is necessary to use an existing chlorination unit to produce chlorine
dioxide

back 165

A diaphragm pump, solution tank, mixer, chlorine dioxide generating tower, and electrical controls.

front 166

What hazards are associated with the handling of sodium chlorite

back 166

It is very combustible around organic compounds.

front 167

What factors could increase the maintenance record needed on chlorine dioxide generators

back 167

Dirty water, hard water, or wet chlorine.

front 168

How often should treated water residual chlorine measurements be made

back 168

At least three times per day on small systems and once every two hours on large systems.

front 169

What methods are used to measure chlorine residual in treated water

back 169

amperometric titration and DPD tests

front 170

What does an ORP probe measure in a disinfection system

back 170

A direct measure of the disinfecting power of a chlorine residual.

front 171

What happens to a microorganism when it loses an electron

back 171

They become inactivated and can no longer transmit a disease or reproduce.

front 172

What maintenance is required on ORP probes

back 172

Cleaning the unit’s sensor once a month.

front 173

What properties make chlorine gas so hazardous

back 173

Flooring gas is 2 ½ times heavier than air extremely toxic and corrosive in moist atmospheres

front 174

What type of breathing apparatus is recommended when repairing chlorine leaks

back 174

A self contained breathing apparatus

front 175

What first aid measures should be taken if a person comes in contact with chlorine gas

back 175

leave the area and remove any clothing that might contain chlorine gas. In extreme cases call 911 then begin treating the victim.

front 176

What happens when ultraviolet radiation is absorbed by the cells of microorganisms

back 176

It damages the genetic material in such a way that the organisms are no longer able to grow or reproduce

front 177

What are the three types of electrode type lamps used to produce UV radiation or UV light

back 177

low pressure low intensity, low pressure high intensity, medium pressure high intensity

front 178

What is a ballast

back 178

A type of transformer that is used to limit the currents to a UV lamp.

front 179

How is the number of UV banks per channel determined

back 179

The required UV dosage to achieve the target effluent quality

front 180

How are UV lamps installed when it is necessary to maintain within the water transmission system

back 180

UV lamps can be installed in a closed pressure vessel

front 181

What kinds of damage can the light from a UV lamp do to operators

back 181

skin burns

front 182

The UV light intensity that reaches the pathogens in the water is affected by which factors

back 182

The condition of the UV lamps and the quality of the water.

front 183

The UV unit automatically adjusts UV dose according to which factors

back 183

Based on the received dose, derive from flow and input from the intensity sensors

front 184

How is the UV dose calculated

back 184

The intensity of the UV radiation and the contact time

front 185

Why do operaters need to periodically observe the UV wiping process

back 185

To ensure proper operation of the wiping action of a bank and the proper wiping cycle

front 186

What’s preliminary steps should be followed when shutting down or starting up a UV disinfection process

back 186

Applying ahead check switches clean units prepare equipment and set
controls

front 187

How can UV light bulbs be cleaned

back 187

in an acid bath in a cleaning tank

front 188

Why must operators monitor the lamp output intensity

back 188

UV lamp burn time

front 189

What influent and effluent characteristics must be monitored

back 189

to ensure Adequate disinfection is performed by the UV lamps

front 190

Why do UV systems require extensive alarm systems

back 190

to ensure continuous complete disinfection of the water being treated

front 191

What tasks are included in the routine maintenance of UV disinfection systems

back 191

Cleaning the quartz sleeves and changing the lamps

front 192

How often should quartz sleeves be cleaned

back 192

Will depend on the quality of the water being treated and the treatment chemicals used before disinfection

front 193

What factors influence the service life of UV lamps

back 193

the the level of suspended solids in the water to be disinfected, the frequency of on/off cycles, and the operating temperature of the lamp electrodes.

front 194

How can operators determine the proper way to dispose of used UV lamps

back 194

Contacting the appropriate Regulatory agency to determine the proper way to dispose of used UV lamps

front 195

What factors influence the effectiveness of ozone disinfection

back 195

The susceptibility of the target organisms, the contact time, and the concentration of the ozone.

front 196

What are the key process control guidelines for ozone disinfection

back 196

dose, mixing, and contact time.

front 197

Why is ozone generated on site

back 197

it is very unstable and decomposes to elemental oxygen in a short time after generation.

front 198

List the problems that can be created by corrosive waters

back 198

Rusty water stained laundry bad taste and internal corrosion of pipes

front 199

What is an electrochemical reaction

back 199

Chemical change is produced by electricity or the production of electricity by chemical changes

front 200

What happens to an iron water pipe when the pipe is connected to a copper pipe

back 200

The iron will corrode if water contains dissolved oxygen and the copper will be protected.

front 201

What is the dezincification of brass

back 201

when brass corrodes leaving behind copper

front 202

What happens when copper and lead solder are in contact

back 202

The lead becomes the anode and will corrode in preference to the copper

front 203

What is a dangerous corrosion inhibitor

back 203

Inhibitors that act on the anode reaction because if there is not enough inhibitor added severe pitting will result and corrosion will be worse than if none had been added.

front 204

What will happen if a copper service line is connected to a steel water main

back 204

corrosion will occur at the anode.

front 205

What effect of stray current corrosion may be evident to homeowners

back 205

When pitting penetrates fixtures or pipes resulting in leaks.

front 206

What causes erosion corrosion in copper tubing

back 206

High velocities

front 207

List the chemical factors that influence corrosion

back 207

PH alkalinity chlorine residual levels of dissolved solids dissolved gases and the types and concentrations of various minerals present in the water

front 208

Why does water with a higher dissolved solids content have a greater potential for corrosion

back 208

Solids dissolved in water are present as ions and increase salt content of the water increasing conductivity

front 209

What is the impact of calcium carbonate on corrosion

back 209

It acts as a corrosion control measure

front 210

What is the most common type of corrosion cell

back 210

Oxygen concentration cell

front 211

Where can an oxygen concentration cell be started

back 211

In the dead end of a water main

front 212

How can pits be started on a metallic surface underwater

back 212

Anything that will shield the metal surface from dissolved oxygen in the water

front 213

What is a tubercle

back 213

A Mound of iron rust

front 214

Why is corrosion of water system facilities a public health concern

back 214

To protect the public from the harmful effects of lead copper or other toxic metals in drinking water

front 215

How can corrosion rates be measured

back 215

By inserting special steel specimens called coupons in the water mains. After a period of time the coupons are removed and the loss of weight and nature of corrosion damage are measured.

front 216

How can leaks in pipes be detected

back 216

The observation of wet spots above a pipeline

front 217

How can you detect a film of calcium carbonate that is too thin to see

back 217

when they drop of dilute hydrochloric acid is placed on an obvious cathodic area

front 218

What does a loss of dissolved oxygen in the water flowing in a distribution system indicate

back 218

N/A

front 219

What toxic metals may enter drinking waters from the customer’s plumbing due to corrosive
water

back 219

N/A

front 220

When is a water considered stable

back 220

When it is just saturated with calcium carbonate

front 221

How can water be tested to determine if it is under saturated or supersaturated with calcium carbonate

back 221

The CCPP or the Langelier index

front 222

The Langelier index is determined by what equation

back 222

Langelier index = pH - pHs

front 223

What is the meaning of pHs

back 223

pH at which water having the same alkalinity and calcium content is just saturated with calcium carbonate

front 224

Why do some waters not have a meaningful pHs value

back 224

They have a low calcium content and alkalinity

front 225

What do rusty or red water complaints indicate

back 225

Where they are occurring and how they can be corrected

front 226

How can the corrosivity of a water be reduced

back 226

Treating the water with chemicals so that it is saturated or slightly supersaturated with calcium carbonate

front 227

What chemicals may be added to waters to reduce the corrosivity

back 227

Quicklime, hydrated lime, soda ash, and caustic soda

front 228

What chemicals may be required for corrosion control if the product of calcium hardness multiplied by the alkalinity Is less than 1000

back 228

Calcium and carbonate

front 229

What chemicals will be required for corrosion control if the product of calcium hardness multiplied by the alkalinity is greater than 5000

back 229

caustic soda or lime

front 230

How can the proper chemical dose be determined to produce water that is just saturated with calcium carbonate

back 230

May be determined graphically or by a trial and error calculation that is practical only with the help of a computer

front 231

List one advantage and one limitation of using zinc compounds instead of lime or caustic for corrosion control

back 231

scaling is reduced (water hardness)

front 232

Where is the application of cathodic protection practical in water treatment plants

back 232

reduce corrosion of metal to water or soil.

front 233

What is the best measure of the corrosivity of soil

back 233

soil resistivity measured using a soil resistance meter

front 234

How can electrolysis of water mains be caused by other utilities

back 234

stray currents generated by cathodic protection installed by other utilities.

front 235

How can internal pipe corrosion be detected and controlled

back 235

detected through rusty water complaints and examining the pipes for pitting/tubercles/corrosion evidence, must be treated to achieve calcium carbonate saturation.

front 236

How can external pipe corrosion be detected and controlled

back 236

indicate by pinhole leaks or rust on outside of pipes, cathodic protection can suffice, or have the pipe replaced with PVC/plastic pipes, cement coated line

front 237

List the important elements of the 1991 lead and copper rule

back 237

MCL goals, monitor lead, treatments for lead/copper, public notification and education, utilities record keeping and reporting, variances and exemptions regulations and compliance schedules based on population size.

front 238

What is the definition of an action level in the lead and copper rule

back 238

value measured in the 90 th percentile at the consumer’s tap

front 239

What are the accepted potable water corrosion control treatments

back 239

N/A

front 240

How do chemical inhibitors control lead and copper in water distribution systems

back 240

providing s coating that prevents corrosion

front 241

How must a utility attempt to educate the public if it fails to meet the lead action level

back 241

EPA developed public education program must be initiated

front 242

How frequently may taste and odor problems occur at a water treatment plant

back 242

They may occur locally on a persistent seasonal occasional or infrequent basis

front 243

What are the most common types of water quality complaints received by a water utility

back 243

Taste odor and colored water

front 244

What is the most damaging effect of problems for a water utility

back 244

The loss of public confidence in the water utilities ability to provide a safe high quality water

front 245

List the major causes of tastes and odors in a water system

back 245

geosmin, MIB, chlorine, chloramines, aldehydes, phenols and chlorophenols

front 246

Where could conditions develop in a water system

back 246

Algal blooms and source waters disinfectants used and the water distribution system

front 247

Which two compounds can produce earthy and musty odors in the water

back 247

geosmin and MIB

front 248

Which inorganic chloramine causes the least odor problems in treated water

back 248

Trichloramine

front 249

Name two groups of bacteria that are known to produce compounds in water

back 249

actinomycetes

front 250

What common blue green algae are associated with odors ranging from earthy musty to septic

back 250

anabaena, aphanizomenon, oscillatoria, microcystis

front 251

What are the two general ways in which microbial populations can contribute to unpleasant tastes and odors in water

back 251

Metabolic byproducts and cellular material of common aquatic microorganisms

front 252

Why does water sometimes have better qualities before treatments than after treatment

back 252

When cells die they rupture and cellular material is released into the water

front 253

When should the application of an algicide be considered

back 253

When the dominant algae is identified as a producer, when algae is not a dominant organism in the population, And sensory or chemical analysis indicates an increase in the order of the water

front 254

What types of minerals in runoff waters can lead to oxygen depletion

back 254

Nitrogen and phosphorus

front 255

How can the nutrient levels in a water supply be increased

back 255

reuse of sludge lagoons

front 256

What causes the diurnal dissolved oxygen cycle

back 256

Algae that produce and consume oxygen

front 257

What factors can cause contamination of a water supply by septic tank and leach field systems in rural areas and in resort and vacation developments

back 257

they may be located too close to rivers and improperly set

front 258

How can industrial waste discharges cause taste and odor problems

back 258

Directly adding odorous compounds such as phenols and aromatic hydrocarbons to the water and adding nutrients that result in causing algal blooms

front 259

What are the sources of most chemical spills

back 259

The result of accidents at industrial plants chemical storage facilities or during transportation

front 260

Why are many municipal water intake facilities located upstream from major agricultural areas

back 260

To avoid possible termination of the water supply by fertilizers microbial contaminants pesticides and herbicides

front 261

List some sources of agricultural wastes that may cause problems in a water supply

back 261

animal wastes, Previously applied fertilizers pesticides herbicides and the spreading agent used to apply them

front 262

How do debris and sludge cause tastes and odors

back 262

microorganisms grow in the organic material

front 263

What parts of the plants are likely locations for algal colonization

back 263

In the sedimentation basin and filter walls and weirs

front 264

What are the most likely sources for the development of tastes and odors

back 264

Any part of the system that are used to store transport or regulate untreated water may provide a suitable habitat for organisms that produce objectionable tastes and odors due to an absence of chlorine residual

front 265

What kind of survey is used to identify the sources of tastes and odors in raw water

back 265

sanitary survey

front 266

How do the chemicals used in a water treatment plant interfere with a search for the source of tastes and odors

back 266

Treatment chemicals such as chlorine and powdered activated carbon tend to mask any changes in quality that may be occurring within the plant

front 267

Where are the potential sources of tastes and odors within a water treatment plant

back 267

Algal growth due to poor housekeeping practices

front 268

What are the main causes of tastes and odors in the distribution system

back 268

Microbiological activity, disinfection residuals and their byproducts, organic or mineral compounds from system materials, and external contaminants from cross connections

front 269

What types of complaints would alert you to the potential of a cross connection

back 269

Complaints about a musty septic or other strange odor in the water

front 270

Which two components should be incorporated into a taste and odor monitoring program

back 270

Routine counting and identification of source water algal populations and attached algae in the

front 271

plant, and sensory analysis such as a taste threshold test of source and distribution system waters and plant profiles when needed

back 271

N/A

front 272

What happens when settled sledges and other debris are allowed to accumulate in the bottoms of channels and tanks in a water treatment plant

back 272

these areas will become septic and impart a foul taste and odor to the water

front 273

When are portions of water treatment plants usually taken out of service for inspection and cleaning while the remainder of the plant continues to operate

back 273

During the winter months when flows are lower and a full plant capacity is not needed to meet water demands

front 274

Why should treatment equipment be capable of operating properly at all times

back 274

The
prevention of episodes at the consumers tap

front 275

What sensory method uses a trained panel to identify tastes and odors in both the treatment process and distribution system

back 275

The taste threshold test

front 276

List the two broad categories of taste and odor treatment methods

back 276

Removal and destruction

front 277

How does the use of chlorine influence taste and odors when water contains algae

back 277

It leads to an increase in odor to to the destruction of algal cells by chlorine

front 278

How can tastes and odors caused by algae be removed most economically in a water treatment plant

back 278

Through the use of improved coagulation

front 279

Aeration is best suited for treating what type of taste and odor problems

back 279

reduced inorganic compounds such as ferrous iron or manganous manganese

front 280

What are the two basic ways that aeration systems can be designed

back 280

passing water through the air or passing air through the water

front 281

What types of odors can often be decreased significantly by chlorination

back 281

N/A

front 282

Under what circumstances might the use of chlorine be the wrong treatment for a taste and odor problem

back 282

N/A

front 283

How would you respond to a permanganate overdose

back 283

Adding powdered activated carbon or increasing the pH

front 284

Why must permanganate storage facilities be dry and well ventilated

back 284

Moisture can cause caking of the material

front 285

Why are adequate permanganate dust control and ventilation importance for equipment protection

back 285

Prevents breathing in of the dust which is irritating to the eyes mucous
membranes and skin

front 286

Why should laboratory and pilot scale testing of the effectiveness of ozonization as a taste and odor control process be conducted before full scale installation

back 286

Due to the specialized equipment requirements

front 287

Why must chlorine dioxide be generated on site

back 287

it is highly unstable

front 288

What types of taste and odor producing wastes have been treated successfully by using chlorine dioxide

back 288

industrial pollution

front 289

What two forms of activated carbon are used in water treatment

back 289

Powdered activated carbon or granular activated carbon

front 290

What terms are used to describe the adsorptive capacities or ratings of activated carbons

back 290

The basis of a phenol number or an iodine number

front 291

Why should PAC be applied at the plant flash mixing facilities

back 291

Carbon must contact the material to be removed for adsorption to occur

front 292

What would you do if a caked layer of carbon starts to form on the surface of the water in the slurry tank

back 292

The cake can be broken up using breaker bars or wooden paddles

front 293

What precautions must operators take because powdered activated carbon is so abrasive

back 293

Equipment used to feed PAC often requires more frequent inspection cleaning and
maintenance

front 294

What adjustments would you make if PAC tends to cake on the surface of the filters

back 294

adjustments to improve PAC removal in the settling process

front 295

How can carbon penetration through a filter be detected

back 295

collect a one liter sample of filter effluent and filter it through a 0.45 picometer membrane filter

front 296

What is empty bed contact time in a granular activated carbon filter

back 296

The time that the water is actually in the filter bed

front 297

What information should be recorded on a water quality complaint form

back 297

name and address of complaints location and description of complaint comments of field investigator response actions and conclusions

front 298

How should operators be kept informed of taste and odor problems

back 298

Through a standard notification procedure for complaints

front 299

What tests can operators conduct to identify problems before they reach the consumer

back 299

Routine testing of raw and finished water for quality

front 300

What factors could cause taste and odor complaints in the local area of a distribution system-

back 300

N/A

front 301

Which locations in a water supply system might contribute problem

back 301

Raw water source storage facilities raw water transmission systems and facilities at a treatment plant

front 302

Why is it important to write out an updated list of options available for treating problems

back 302

N/A

front 303

What two analysis can be used as an early warning system for taste and odor events

back 303

Routine monitoring of algal populations in conjunction with the use of sensory analysis in the form of tastes threshold test

front 304

List the five types of primary contaminants considered to be of public health importance

back 304

Inorganic contaminants, Organic contaminants, turbidity, microbial contaminants, and radiological contaminants

front 305

What criteria must be met before EPA selects a contaminant for regulation

back 305

The contaminants may have an adverse effect on the health of the people, it is known to occur or there’s a high chance it will occur in PWS often enough and at levels of public health concern, And regulation of the contaminants presents a meaningful opportunity for health risk reductions for people served by PWS

front 306

What is the purpose of a consumer confidence report rule

back 306

To improve public Health Protection by providing educational material to allow consumers to make educated decisions regarding any potential health risks pertaining to the quality treatment and management of their drinking water supply

front 307

Why are treatment technique requirements also referred to as primary standards rather than as MCLs

back 307

Testing for certain contaminants can be expensive requiring specific treatment
techniques

front 308

Why is arsenic listed as a primary contaminant

back 308

N/A

front 309

Why is nitrate in drinking water above the national standard of 10 mg/L considered an immediate threat to public health

back 309

it causes blue baby syndrome

front 310

What is the purpose of the TCR

back 310

It is the limit of total coliforms in drinking water

front 311

What is the most basic test for bacterial contamination of a water supply

back 311

test for total coliform bacteria

front 312

What does the final RTRC establish

back 312

MCL for E. Coli

front 313

What Organism is most implicated in US waterborne disease outbreaks

back 313

Giardia lamblia

front 314

How do regulation treatments techniques ensure that harmful organisms are treated

back 314

N/A

front 315

Why substitute chlorine residual testing for some of the bacteriological testing

back 315

It could give a quicker indication of the condition of the system

front 316

What is often the most corrosive chemical found in a water plant

back 316

N/A

front 317

What is one important safety precaution that should be followed at a water treatment plant

back 317

N/A

front 318

What are the symptoms of fluoride poisoning

back 318

N/A

front 319

What is the first aid procedure for skin contact with fluoride

back 319

N/A

front 320

What special training must be given to all operators who handle fluoride compounds

back 320

N/A

front 321

List the compounds most commonly used to fluoridate water

back 321

N/A

front 322

List the compounds most commonly used to fluoridate water

back 322

N/A

front 323

Which is the easiest fluoridation chemical to feed

back 323

N/A

front 324

List examples of solution feeders for liquid fluoridation chemicals

back 324

N/A

front 325

What important aspects should be incorporated into the design of a water treatment plant

back 325

N/A

front 326

Why is sodium silicofluoride not recommended to feed through a saturator

back 326

N/A

front 327

What is a saturator

back 327

N/A

front 328

Describe a downflow/upflow saturator

back 328

N/A

front 329

How can you see the level of undissolved sodium fluoride in an upflow saturator

back 329

N/A

front 330

List the types of alarms at a fluoridation plant

back 330

N/A

front 331

List the different parts of a small hydrofluosilicic acid system

back 331

N/A

front 332

Why should an operator avoid injecting solution into the top of a small hydrofluosilicic acid system pipe

back 332

N/A

front 333

What type of feeding system is typically found in a large hydrofluosilicic acid system

back 333

N/A

front 334

Why should hydrofluosilicic acid storage tanks made of plastic be housed in enclosures

back 334

N/A

front 335

What is one result of using a closed loop control system in an unattended plant using a fluoride analyzer as one of the controls

back 335

N/A

front 336

When performing the final equipment checkup, what must the operator be certain of

back 336

N/A

front 337

When reviewing fluoride feeding system designs and specifications, what should the operator check

back 337

N/A

front 338

Why must corrosion resistant drop pans and drains be provided with a fluoride feeding system

back 338

N/A

front 339

Why use alarms with a fluoride feeding system

back 339

N/A

front 340

Why must the proper position for all valves be determined in the industrial feeder startup procedure

back 340

N/A

front 341

Why record the amount of chemical left in the storage bin

back 341

N/A

front 342

After a plant shutdown, which meter provides equipment information

back 342

N/A

front 343

What benefits do the equipment manufacturer’s manuals for procedures provide

back 343

N/A

front 344

What are the benefits of overfeeding chemicals

back 344

N/A

front 345

Why should fluoridation equipment be cleaned out of the equipment is going to be shut down for an extended length of time

back 345

N/A

front 346

How can fluoride dust be removed from gears

back 346

N/A

front 347

During maintenance of fluoridation equipment, how concerned should you be about checking the feed rate by catching a given amount of fluoride over time

back 347

N/A