Wastewater Treatment Operations

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182 Terms

1
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Ideal velocity for sanitary sewer collection systems

2 ft/sec

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Typical distance between manholes

300-500 ft

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Purpose of preliminary treatment processes

Remove course material from wastewater

4
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Purpose of primary treatment processes

Remove settleable and floatable materials

5
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Purpose of secondary treatment processes

Remove suspended and dissolved solids

6
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Sulfur dioxide (SO2) is used for...

Used to neutralize chlorine & detoxify the effluent

7
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Ideal flow-through velocity of a grit channel

0.7-1.4 ft/sec

1 ft/sec is best

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Types of flow measuring devices in an open channel

Parshall Flume & V-notch weir

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Types of flow measuring devices in a closed channel

Venturi meter & magnetic flowmeter

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Advantages of measuring flow with a Parshall flume

Smooth constriction

no protruding edges

waste will not collect behind the metering device

11
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Ideal detention time in a primary clarifier

1.5-2 hrs

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Humus

Layer of organisms (aka biomass) on trickling filter media that eventually gets thick enough to slough off and must be removed by settling in the secondary clarifier

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Typical BOD & suspended solids removal rate of an activated sludge plant

90-99% removal

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Mixed liquor

Activated sludge + raw wastewater + return sludge in an aeration tank

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Types of bacteria present in a digester

Acid formers & gas formers

16
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Typical organic matter removal rate of a digester

50% removal

17
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If temperature is kept at 95F, what is the typical digestion time in a digester?

30 days

18
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Byproducts of digestion

Organic acids

carbon dioxide gas

methane

19
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Typical gas ratio in a digester

70% methane, 30% CO2

20
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Types of dewatering methods

sludge drying beds

lagoons

centrifuges

vacuum filters

filter presses

21
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Shallow pond

Aerobic

3-6 ft deep

Oxygen throughout their depth

22
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Deep pond

Anaerobic

8-12 ft deep

Treatment depends on fermentation of sludge at the bottom

Odorous

Mainly for industrial waste

23
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Facultative pond

Most common type of pond

Top layer is aerobic

Bottom layer is anaerobic

Algae supplies oxygen to supernatant

24
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Short-circuiting

When flowing water entering a tank or basin flows along a nearly direct pathway from inlet to outlet, resulting in shorter contact or settling times

25
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Bar Racks

Spacing between bars is 3-4 in

Usually found in bypass channels

Manually cleaned

26
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Bar Screens

Spacing between bars is 3/8-2 in

27
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The more debris that collects on bar screens leads to...

Greater head loss through bar screens

Organic wastes settled out

Dissolved oxygen is depleted

Septic conditions

28
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Shear pin

A straight pin that will break when a certain load or stress is exceeded

29
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Typical limit of allowable head loss at a bar screen

3 in of head loss

30
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Benefits of a communitor

Reduction in screenings disposal

Reduction in flies

Reduction in odors

31
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Most grit channels are designed to remove...

0.2 mm size sand & and all other heavier materials

32
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Typical settling rate of sand (0.2 mm)

0.075 ft/sec

33
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Settling time (sec) =

Depth (ft) / Settling Rate (ft/sec)

34
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Grit channel length (ft) =

[Depth of channel (ft) x Flow velocity (ft/sec)] / Settling Rate (ft/sec)

35
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If inspection of grit reveals a high amount of organic material...

Velocity in the grit channel may be too low

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If inspection of grit reveals mainly large or heavy sand...

Velocity in the channel may be too high

37
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Aerated grit chambers work on the basis of...

Air and water have a lower specific gravity than water, so grit settles out better

38
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What is a slurry?

A watery mixture or suspension of insoluble matter

39
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How does a cyclone grit separator work?

Water and suspended particles are carried upward in the secondary vortex while heavy particles move outward and down in the primary vortex.

40
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Typical grit quantities per volume wastewater

1-4 cubic ft / 1 MG

41
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When disposing of grit by burial, how much soil should cover the grit?

6 in

42
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What are the benefits of pre-aerating wastewater before grit removal?

Improve grit removal efficiency

Freshen wastewater

Remove gases

Add oxygen

Promote flotation of grease

Aid coagulation

43
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Primary sludges are usually ______ than secondary sludges

Denser

44
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Types of sludge handling and disposal

Sludge digestion

Vacuum filtration

Filter presses

Incineration

Land disposal

Lagoons

Burial

45
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Surface Loading (GPD/sq ft) =

Flow (gal/day) / Surface Area (sq ft)

46
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Detention time (hr) =

[Tank Volume (cu ft) x 7.48 gal/cu ft x 24 hr/day] / Flow (gal/day)

47
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Recommended analyses for a primary clarifier

Settleable solids

Suspended solids

BOD

DO (effluent only)

pH

Temperature (influent only)

48
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Ideal velocity in a primary clarifier

1.0-2.0 ft/min

49
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Factors that influence settling characteristics in a primary clarifier

Temperature

Short circuits

Detention time

Weir overflow rate

Surface loading rate

Solids loading

50
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What is the importance of knowing the weir overflow rate in a clarifier?

To prevent short circuits or high velocity near the weir, which might pull settling solids into the effluent

51
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Weir Overflow Rate (GPD/ft) =

Flow (GPD) / Length of Weir (ft)

52
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Recommended weir overflow rate for a primary clarifier

10,000-20,000 GPD/linear ft of weir

53
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Recommended surface loading rate in a clarifier

300-1200 GPD/sq ft

54
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Solids loading (lbs/day/sq ft) =

[Flow (MGD) x MLSS (mg/L) x 8.34 lbs/gal] / Surface Area (sq ft)

55
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Typical solids loading in a secondary clarifier

12-30 lbs/day/sq ft

56
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Rationale for secondary clarifiers

Biological treatment processes convert additional solids to the settleable form and also produce floc containing microorganisms

57
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The sludge volume in the secondary tank will be _____ from the activated sludge process than from the trickling filter process

Greater

58
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Typical detention time for a secondary clarifier

2-3 hrs

59
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Typical weir overflow rate for a secondary clarifier

5000-15000 GPD/lineal ft

60
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Typical return sludge rates at an activated sludge plant

10-50% of plant inflow

61
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Recommended analyses for a secondary clarifier

Suspended solids

Turbidity

DO

pH

BOD

Ammonia Nitrogen

Sludge levels

62
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What is a sedimentation-digestion unit?

A type of package treatment plant which combines a small clarifier over a sludge digester

63
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Chemical added to wastewater to raise the pH in a digester

Lime or anhydrous ammonia

64
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In a sedimentation-digestion unit, how often should you remove supernatant?

Twice a day for 15-30 min

65
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In a sedimentation-digestion unit, how often should you remove sludge?

Start wasting when solids start to appear in the supernatant

Stop wasting when sludge starts to run thin

66
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What type of dewatering process is typical for a sedimentation-digestion unit?

Sand drying beds

67
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Ideal temperature range for a digester

80-95 degrees F

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Recommended analyses for a sedimentation-digestion unit

Inflow

Suspended solids

Settleable solids

BOD (optional)

Temperature

pH

Quantity of sludge withdrawn

Chlorine residual (effluent)

69
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What is an Imhoff tank?

A conical tank that combines sedimentation and digestion in the same unit

70
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Typical detention time in a septic tank

12-24 hrs

71
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What are colloids?

Small, finely divided solids that remain dispersed in a liquid for a long time due to their size and electrical charge

72
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Describe nitrification

An aerobic process

Bacteria oxidize ammonia and organic nitrogen in wastewater into nitrate

First stage BOD is called carbonaceous BOD

Second stage BOD is called nitrogenous BOD

73
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Describe denitrification

Anoxic biological reduction of nitrate/nitrate nitrogen to nitrogen gas

Nitrogen bubbles attach to the floc and float

Common cause of rising sludge in secondary clarifiers

74
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What is ponding?

A condition occurring on trickling filters

When hollow spaces become plugged

Water is unable to pass through the filter media

Result of excessive slime growth, trash, or media breakdown

75
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Typical suspended solids and BOD removal efficiency of secondary treatment

90% or more

76
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List the components of a trickling filter

Media

Underdrain system

Distribution system

77
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Typical size of rock media in a trickling filter

2-4 in wide

Uniform in size

3-8 ft deep

Void space is 35% of filter media

78
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Typical size of synthetic media in a trickling filter

15-30 ft deep

Void space is 95% of filter volume

79
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Advantages of recirculation in a trickling filter

Increased efficiency

Dilutes strength of wastewater

Prevents excessive buildup of slime growths

Helps seed lower portions of filter with active organisms

Helps keep biofilm healthy during low flow

Addition of DO

Controls flies

80
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Advantage of synthetic media

Considerably more surface area per unit of dead space for slime to accumulate

81
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What effect does warm temperature have on a trickling filter?

Organisms are more active

Higher loadings

Greater efficiency is possible

82
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What is hydraulic loading?

The total volume of liquid (including recirculation) applied to a filter

Expressed as GPD/sq ft

83
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What is organic loading?

The weight of BOD applied per day per 1000 cubic feet of filter media

Expressed as lbs BOD/day/1000 cu ft

84
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Typical hydraulic loading of a standard-rate trickling filter

25-100 GPD/sq ft

85
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Typical organic loading of a standard-rate trickling filter

5-25 lbs BOD/day/1000 cu ft

86
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What is a roughing filter?

A high-rate trickling filter that receives a very high organic loading (100-300 lbs/day/1000 cu ft)

87
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What should you check before starting a trickling filter?

Replace packing grease of filter bearings

Correct oil is used

Distributor arms are level

No foreign objects in fixed-spray nozzles

No debris in underdrain system

Valves operate smoothly

88
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Why should you record the speed of rotation of a trickling filter distributor arm during initial start-up?

The distributor arm speed is proportional to the influent flow rate

Provides a reference for daily inspection and operation of distributor arm

89
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Typical time for slime to build up on trickling filter media

Several days for slime growth to start

Several weeks for fully developed slime

90
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How can you speed up the development of slime growth on a trickling filter?

Recirculate wastewater prior to treating the main wastewater flow stream

Add waste activated sludge

91
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Recommended daily observations in a trickling filter plant

Indications of ponding

Filter flies

Odors

Plugged orifices

Roughness/vibration of distributor arms

Leakage past the distributor turntable seal

Splash beyond filter media

Cleanup of slimes not on media

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Where should recirculation take place at a trickling filter plant and why?

Primary clarifier

Adds oxygen to incoming waste-stream

Prevents odors

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Recommended analyses for a trickling filter

DO (final effluent & filter underflow)

Settleable solids

pH

Temperature

BOD

Suspended solids

Chlorine residual (final effluent)

Coliform bacteria (final effluent)

Clarity (final effluent)

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Advantage of performing COD analyses over BOD analyses

4 hrs to obtain results vs 5 days

95
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Nutrient requirements of a trickling filter

For each incoming 100 lbs of BOD, there should be 5 lbs of ammonia nitrogen and 1 lb of orthophosphate

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Advantages of a trickling filter

Less operating attention

Shock loads are less frequent because recovery is faster

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Operational challenges of using a trickling filter

Ponding

Odors

Flies

Freezing

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Major operational consideration/strategy at a trickling filter plant

Use the lowest possible recirculation rate that will produce good results

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Operational criteria for a trickling filter plant

Hydraulic loading rate

Organic loading rate

100
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Recommended DO concentration of trickling filter effluent

3-6 mg/L (rock)

4-8 mg/L (synthetic)