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Water and wastewater treatment processes ENV H 452/ENV H 542 John Scott Meschke Office: Suite 2249, 4225 Roosevelt Phone: 206-221-5470 Email: [email protected] du Gwy-Am Shin Office: Suite 2339, 4225 Roosevelt Phone: 206-543-9026 Email: [email protected]
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Water and wastewater treatment processes ENV H 452/ENV H 542 John Scott Meschke Office: Suite 2249, 4225 Roosevelt Phone: 206-221-5470 Email: [email protected].

Dec 22, 2015

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Page 1: Water and wastewater treatment processes ENV H 452/ENV H 542 John Scott Meschke Office: Suite 2249, 4225 Roosevelt Phone: 206-221-5470 Email: jmeschke@u.washington.edu.

Water and wastewater treatment processes

ENV H 452/ENV H 542

John Scott Meschke

Office: Suite 2249,

4225 Roosevelt

Phone: 206-221-5470

Email: [email protected]

Gwy-Am Shin

Office: Suite 2339,

4225 Roosevelt

Phone: 206-543-9026

Email: [email protected]

Page 2: Water and wastewater treatment processes ENV H 452/ENV H 542 John Scott Meschke Office: Suite 2249, 4225 Roosevelt Phone: 206-221-5470 Email: jmeschke@u.washington.edu.

Key points

• Purpose of the individual unit processes

• The typical operating conditions

• The outcome of the processes

• Microbial reduction in the processes

Page 3: Water and wastewater treatment processes ENV H 452/ENV H 542 John Scott Meschke Office: Suite 2249, 4225 Roosevelt Phone: 206-221-5470 Email: jmeschke@u.washington.edu.

Wastewater treatment processes

Page 4: Water and wastewater treatment processes ENV H 452/ENV H 542 John Scott Meschke Office: Suite 2249, 4225 Roosevelt Phone: 206-221-5470 Email: jmeschke@u.washington.edu.

How much wastewater do we produce each day?

Wastewater Characteristics

Source Average Daily FlowDomestic sewage 60-120 gal/capitaShopping centers 60-120 gal/1000 ft2 total floor

areaHospitals 240-480 gal/bedSchools 18-36 gal/studentTravel trailer parks

Without individualhookups

90 gal/site

With individualhookups

210 gal/site

Campgrounds 60-150 gal/campsiteMobile home parks 265 gal/unitMotels 40-53 gal/bedHotels 60 gal/bedIndustrial areas

Light industrial area 3750 gal/acreHeavy industrial 5350 gal/acre

Source: Droste, R.L., 1997. Theory and Practice ofWater and Wastewater Treatment

These values are rough estimates only and vary greatly by locale.

Page 5: Water and wastewater treatment processes ENV H 452/ENV H 542 John Scott Meschke Office: Suite 2249, 4225 Roosevelt Phone: 206-221-5470 Email: jmeschke@u.washington.edu.

Wastewater treatment systems

• Decentralized– Septic tank– Waste stabilization ponds

• Facultative lagoon• Maturation lagoon

– Land treatment

• Centralized

Page 6: Water and wastewater treatment processes ENV H 452/ENV H 542 John Scott Meschke Office: Suite 2249, 4225 Roosevelt Phone: 206-221-5470 Email: jmeschke@u.washington.edu.

Sewer systems

Page 7: Water and wastewater treatment processes ENV H 452/ENV H 542 John Scott Meschke Office: Suite 2249, 4225 Roosevelt Phone: 206-221-5470 Email: jmeschke@u.washington.edu.

Typical composition of untreated domestic wastewater

Page 8: Water and wastewater treatment processes ENV H 452/ENV H 542 John Scott Meschke Office: Suite 2249, 4225 Roosevelt Phone: 206-221-5470 Email: jmeschke@u.washington.edu.

Microorganism concentrations in untreated wastewater

Page 9: Water and wastewater treatment processes ENV H 452/ENV H 542 John Scott Meschke Office: Suite 2249, 4225 Roosevelt Phone: 206-221-5470 Email: jmeschke@u.washington.edu.

(Minimum) Goals of wastewater treatment processes

• <30 mg/L BOD5

• <30 mg/L of suspended solids

• <200 CFU/100ml fecal coliforms

Page 10: Water and wastewater treatment processes ENV H 452/ENV H 542 John Scott Meschke Office: Suite 2249, 4225 Roosevelt Phone: 206-221-5470 Email: jmeschke@u.washington.edu.

Conventional Community (Centralized) Sewage Treatment

Pathogen Reductions Vary from: low (<90%) to Very High (>99.99+%)

Secondary Treatment Using Activated Sludge Process

Sludge drying bed or mechanical dewatering process

Page 11: Water and wastewater treatment processes ENV H 452/ENV H 542 John Scott Meschke Office: Suite 2249, 4225 Roosevelt Phone: 206-221-5470 Email: jmeschke@u.washington.edu.

Typical Municipal Wastewater Treatment System

Preliminary or Pre-Preliminary or Pre-TreatmentTreatment

PrimaryTreatment

SecondaryTreatment

Disinfection

Sludge Treatment& Disposal

Page 12: Water and wastewater treatment processes ENV H 452/ENV H 542 John Scott Meschke Office: Suite 2249, 4225 Roosevelt Phone: 206-221-5470 Email: jmeschke@u.washington.edu.

Preliminary Wastewater Treatment System

Preliminary or Pre-Preliminary or Pre-TreatmentTreatment

Solids to Landfill

Page 13: Water and wastewater treatment processes ENV H 452/ENV H 542 John Scott Meschke Office: Suite 2249, 4225 Roosevelt Phone: 206-221-5470 Email: jmeschke@u.washington.edu.

Preliminary Treatment Facilities

Preliminary Treatment - Bar Racks

Bar Racks: are used to remove large objects that could potentially damage downstream treatment/pumping facilities.

Ref: Metcalf & Eddy, 1991

Page 14: Water and wastewater treatment processes ENV H 452/ENV H 542 John Scott Meschke Office: Suite 2249, 4225 Roosevelt Phone: 206-221-5470 Email: jmeschke@u.washington.edu.

Preliminary Treatment - Grit chamber

Grit chamber: used to remove small to medium sized, dense objects such as sand, broken glass, bone fragments, pebbles, etc.

Page 15: Water and wastewater treatment processes ENV H 452/ENV H 542 John Scott Meschke Office: Suite 2249, 4225 Roosevelt Phone: 206-221-5470 Email: jmeschke@u.washington.edu.

Primary Wastewater Treatment

PrimaryTreatmentPrimary

Treatment

Page 16: Water and wastewater treatment processes ENV H 452/ENV H 542 John Scott Meschke Office: Suite 2249, 4225 Roosevelt Phone: 206-221-5470 Email: jmeschke@u.washington.edu.

Primary sedimentation • To remove settleable solids from wastewater

Page 17: Water and wastewater treatment processes ENV H 452/ENV H 542 John Scott Meschke Office: Suite 2249, 4225 Roosevelt Phone: 206-221-5470 Email: jmeschke@u.washington.edu.

Primary Clarification

PrimarySludge

PrimaryEffluent

Influent from Preliminary Treatment

Section through a Circular Primary Clarifier

Primary Treatment

Scum: Oil, Grease, Floatable Solids

Page 18: Water and wastewater treatment processes ENV H 452/ENV H 542 John Scott Meschke Office: Suite 2249, 4225 Roosevelt Phone: 206-221-5470 Email: jmeschke@u.washington.edu.

Primary sedimentation

• To remove settleable solids from wastewater• Maximum flow: 30 - 40 m3 per day• Retention period: 1.5 - 2.0 hours (at maximum flow)• 50 - 70 % removal of suspended solids• 25 - 35 % removal of BOD5

• ~20 % removal of phosphate • ~50 % removal of viruses, bacteria, and protozoa• 90 % removal of helminth ova

Page 19: Water and wastewater treatment processes ENV H 452/ENV H 542 John Scott Meschke Office: Suite 2249, 4225 Roosevelt Phone: 206-221-5470 Email: jmeschke@u.washington.edu.

Secondary Wastewater Treatment

SecondaryTreatmentSecondaryTreatment

Page 20: Water and wastewater treatment processes ENV H 452/ENV H 542 John Scott Meschke Office: Suite 2249, 4225 Roosevelt Phone: 206-221-5470 Email: jmeschke@u.washington.edu.

Secondary treatment processes

• To remove suspended solids, nitrogen, and phosphate

• 90 % removal of SS and BOD5

• Various technologies– Activated sludge process– Tricking filter– Aerated lagoons– Rotating biological contractors

Page 21: Water and wastewater treatment processes ENV H 452/ENV H 542 John Scott Meschke Office: Suite 2249, 4225 Roosevelt Phone: 206-221-5470 Email: jmeschke@u.washington.edu.

Secondary Treatment Using Activated Sludge Process

SecondaryTreatment

Secondary Treatment

Sludge drying bed or mechanical dewatering process

Page 22: Water and wastewater treatment processes ENV H 452/ENV H 542 John Scott Meschke Office: Suite 2249, 4225 Roosevelt Phone: 206-221-5470 Email: jmeschke@u.washington.edu.

The Activated Sludge Process

Aerobic microbes utilities carbon and other nutrients to form a healthy activated sludge (AS) biomass (floc)

The biomass floc is allowed to settle out in the next reactor; some of the AS is recycled

Secondary Treatment

Simplified Activated Sludge Description

Page 23: Water and wastewater treatment processes ENV H 452/ENV H 542 John Scott Meschke Office: Suite 2249, 4225 Roosevelt Phone: 206-221-5470 Email: jmeschke@u.washington.edu.

Activated sludge process

• To remove suspended solids, nitrogen, and phosphate• Food to microorganism ratio (F:M ratio): 0.25 kg BOD5

per kg MLSS (mixed liquor suspended solids) per day at 10 oC or 0.4 kg BOD5 per kg MLSS per day at 20 oC

• Residence time: 2 days for high F:M ratio, 10 days or more for low F:M ratio

• Optimum nutrient ratio: BOD5:N:P =>100:5:1• 90 % removal of BOD5 and SS• ~20 % removal of phosphate• >90 % removal of viruses and protozoa and 45 - 95 %

removal of bacteria

Page 24: Water and wastewater treatment processes ENV H 452/ENV H 542 John Scott Meschke Office: Suite 2249, 4225 Roosevelt Phone: 206-221-5470 Email: jmeschke@u.washington.edu.

Secondary Treatment Using Trickling Filter Process

SecondaryTreatment

Secondary Treatment

TricklingFilter

Page 25: Water and wastewater treatment processes ENV H 452/ENV H 542 John Scott Meschke Office: Suite 2249, 4225 Roosevelt Phone: 206-221-5470 Email: jmeschke@u.washington.edu.

Trickling Filter

http://www.rpi.edu/dept/chem-eng/Biotech-Environ/FUNDAMNT/streem/trickfil.jpg

Primary effluent drips onto rock orman-made media

Rotating arm todistribute water evenly over filter

Rock-bed with slimy (biofilm) bacterial growth

Primary effluent pumped inTreated waste to secondary clarifier

Page 26: Water and wastewater treatment processes ENV H 452/ENV H 542 John Scott Meschke Office: Suite 2249, 4225 Roosevelt Phone: 206-221-5470 Email: jmeschke@u.washington.edu.

Trickling Filter

http://www.eng.uc.edu/friendsalumni/research/labsresearch/biofilmreslab/Tricklingfilter_big.jpg

Page 27: Water and wastewater treatment processes ENV H 452/ENV H 542 John Scott Meschke Office: Suite 2249, 4225 Roosevelt Phone: 206-221-5470 Email: jmeschke@u.washington.edu.

Tricking filter process

• To remove suspended solids, nitrogen, and phosphate

• Organic loading (BOD5 X flow/volume of filter): 0.1 kg BOD5 per m3 per day

• Hydraulic loading: 0.4 m3 per day per m3 of plan area

• 90 % removal of BOD5 and SS• ~20 % removal of phosphate• Variable removal levels of viruses, 20-80 %

removal of bacteria and >90 % removal of protozoa

Page 28: Water and wastewater treatment processes ENV H 452/ENV H 542 John Scott Meschke Office: Suite 2249, 4225 Roosevelt Phone: 206-221-5470 Email: jmeschke@u.washington.edu.

Wastewater Disinfection

Disinfection

Page 29: Water and wastewater treatment processes ENV H 452/ENV H 542 John Scott Meschke Office: Suite 2249, 4225 Roosevelt Phone: 206-221-5470 Email: jmeschke@u.washington.edu.

Wastewater disinfection

• To inactivate pathogens in wastewater

• Several choices– Free chlorine and combined chlorine– UV– Ozone– Chlorine dioxide

Page 30: Water and wastewater treatment processes ENV H 452/ENV H 542 John Scott Meschke Office: Suite 2249, 4225 Roosevelt Phone: 206-221-5470 Email: jmeschke@u.washington.edu.

Overall pathogen reduction in wastewater treatment

Page 31: Water and wastewater treatment processes ENV H 452/ENV H 542 John Scott Meschke Office: Suite 2249, 4225 Roosevelt Phone: 206-221-5470 Email: jmeschke@u.washington.edu.

Water treatment processes

Page 32: Water and wastewater treatment processes ENV H 452/ENV H 542 John Scott Meschke Office: Suite 2249, 4225 Roosevelt Phone: 206-221-5470 Email: jmeschke@u.washington.edu.

Water contaminants

• Chemicals– Inorganics– Organics

• Synthetic organic compounds• Volatile organic compounds

• Microbes– Viruses– Bacteria– Protozoa parasites– Algae– Helminths

Page 33: Water and wastewater treatment processes ENV H 452/ENV H 542 John Scott Meschke Office: Suite 2249, 4225 Roosevelt Phone: 206-221-5470 Email: jmeschke@u.washington.edu.

Water contaminants (I)

Page 34: Water and wastewater treatment processes ENV H 452/ENV H 542 John Scott Meschke Office: Suite 2249, 4225 Roosevelt Phone: 206-221-5470 Email: jmeschke@u.washington.edu.

Water contaminants (II)

Page 35: Water and wastewater treatment processes ENV H 452/ENV H 542 John Scott Meschke Office: Suite 2249, 4225 Roosevelt Phone: 206-221-5470 Email: jmeschke@u.washington.edu.

Water contaminants (III)

Page 36: Water and wastewater treatment processes ENV H 452/ENV H 542 John Scott Meschke Office: Suite 2249, 4225 Roosevelt Phone: 206-221-5470 Email: jmeschke@u.washington.edu.

Water contaminants (IV)

Page 37: Water and wastewater treatment processes ENV H 452/ENV H 542 John Scott Meschke Office: Suite 2249, 4225 Roosevelt Phone: 206-221-5470 Email: jmeschke@u.washington.edu.

Water contaminants (V)

Page 38: Water and wastewater treatment processes ENV H 452/ENV H 542 John Scott Meschke Office: Suite 2249, 4225 Roosevelt Phone: 206-221-5470 Email: jmeschke@u.washington.edu.

Multiple barrier concept for public health protection

Page 39: Water and wastewater treatment processes ENV H 452/ENV H 542 John Scott Meschke Office: Suite 2249, 4225 Roosevelt Phone: 206-221-5470 Email: jmeschke@u.washington.edu.

Barrier Approach to Protect Public Health in Drinking Water

• Source Water Protection

• Treatment Technology

• Disinfection

• Disinfectant residual in distribution system

Page 40: Water and wastewater treatment processes ENV H 452/ENV H 542 John Scott Meschke Office: Suite 2249, 4225 Roosevelt Phone: 206-221-5470 Email: jmeschke@u.washington.edu.

Water treatment processes

Page 41: Water and wastewater treatment processes ENV H 452/ENV H 542 John Scott Meschke Office: Suite 2249, 4225 Roosevelt Phone: 206-221-5470 Email: jmeschke@u.washington.edu.

Oxidation

• To remove inorganics (Fe++, Mn++) and some synthetic organics– Cause unaesthetic conditions (brown color)– Promote the growth of autotrophic bacteria (iron bacteria): taste

and order problem• Free chlorine, chlorine dioxide, ozone, potassium

permanganate– Fe++ + Mn ++ + oxygen + free chlorine → FeOx ↓ (ferric oxides) +

MnO2 ↓ (manganese dioxide)– Fe (HCO3)2 (Ferrous bicarbonate) + KMnO4 (Potassium

permanganase) → Fe (OH)3 ↓ (Ferric hydroxide) + MnO2 ↓ (manganese dioxide)

– Mn (HCO3)2 (Manganese bicarbonate) + KMnO4 (Potassuim permanganase) → MnO2 ↓ (manganese dioxide)

Page 42: Water and wastewater treatment processes ENV H 452/ENV H 542 John Scott Meschke Office: Suite 2249, 4225 Roosevelt Phone: 206-221-5470 Email: jmeschke@u.washington.edu.

Physico-chemical processes

• To remove particles in water

• Coagulation/flocculation/sedimentation

• Filtration

Page 43: Water and wastewater treatment processes ENV H 452/ENV H 542 John Scott Meschke Office: Suite 2249, 4225 Roosevelt Phone: 206-221-5470 Email: jmeschke@u.washington.edu.

Rapid Mix

• Intense mixing of coagulant and other chemicals with the water

• Generally performed with mechanical mixers

Chemical Coagulant

Page 44: Water and wastewater treatment processes ENV H 452/ENV H 542 John Scott Meschke Office: Suite 2249, 4225 Roosevelt Phone: 206-221-5470 Email: jmeschke@u.washington.edu.

Major Coagulants

• Hydrolyzing metal salts– Alum (Al2(SO4)3)

– Ferric chloride (FeCl3)

• Organic polymers (polyelectrolytes)

Page 45: Water and wastewater treatment processes ENV H 452/ENV H 542 John Scott Meschke Office: Suite 2249, 4225 Roosevelt Phone: 206-221-5470 Email: jmeschke@u.washington.edu.

Coagulation with Metal Salts

Al(OH)

Alx(OH)y

Colloid

Al(OH)3

Al(OH)3 Colloid

Al(OH)3

Al(OH)3

Colloid

+ +Soluble Hydrolysis Species

(Low Alum Dose)

Colloid

Colloid

Colloid

Al(OH)3Al(OH)3

Al(OH)3

Al(OH)3

Al(OH)3

(High Alum Dose)

Floc

Sweep CoagulationCharge Neutralization

Page 46: Water and wastewater treatment processes ENV H 452/ENV H 542 John Scott Meschke Office: Suite 2249, 4225 Roosevelt Phone: 206-221-5470 Email: jmeschke@u.washington.edu.

Horizontal Paddle Flocculator

Page 47: Water and wastewater treatment processes ENV H 452/ENV H 542 John Scott Meschke Office: Suite 2249, 4225 Roosevelt Phone: 206-221-5470 Email: jmeschke@u.washington.edu.

Flocculation ExampleFlocculation Example

Water coming from Water coming from rapid mix.rapid mix. Water goes to sedimentationWater goes to sedimentation

basin.basin.

Page 48: Water and wastewater treatment processes ENV H 452/ENV H 542 John Scott Meschke Office: Suite 2249, 4225 Roosevelt Phone: 206-221-5470 Email: jmeschke@u.washington.edu.

Sedimentation Basin

Page 49: Water and wastewater treatment processes ENV H 452/ENV H 542 John Scott Meschke Office: Suite 2249, 4225 Roosevelt Phone: 206-221-5470 Email: jmeschke@u.washington.edu.

Sedimentation Basin ExampleSedimentation Basin ExampleWater coming from Water coming from flocculation basin.flocculation basin.

Water goes to Water goes to filter.filter.

Floc (sludge) collectedin hopperSludge to solids

treatment

Page 50: Water and wastewater treatment processes ENV H 452/ENV H 542 John Scott Meschke Office: Suite 2249, 4225 Roosevelt Phone: 206-221-5470 Email: jmeschke@u.washington.edu.

Coagulation/flocculation/and sedimentation

• To remove particulates and natural organic materials in water• Coagulation

– 20 -50 mg/L of Alum at pH 5.5-6.5 (sweep coagulation)– rapid mixing: G values = 300-800/second

• Flocculation: – Slow mixing: G values = 30-70/second– Residence time:10 -30 minutes

• Sedimentation– Surface loading: 0.3 -1.0 gpm/ft2

– Residence time: 1 – 2 hours• Removal of suspended solids and turbidity: 60-80 %• Reduction of microbes

– 74-97 % Total coliform – 76-83 % of fecal coliform – 88-95 % of Enteric viruses– 58-99 % of Giardia– 90 % of Cryptosporidium

Page 51: Water and wastewater treatment processes ENV H 452/ENV H 542 John Scott Meschke Office: Suite 2249, 4225 Roosevelt Phone: 206-221-5470 Email: jmeschke@u.washington.edu.

Filtration

• To remove particles and floc that do not settle by gravity in sedimentation process

• Types of granular media– Sand– Sand + anthracite– Granular activated carbon

• Media depth ranges from 24 to 72 inches

Page 52: Water and wastewater treatment processes ENV H 452/ENV H 542 John Scott Meschke Office: Suite 2249, 4225 Roosevelt Phone: 206-221-5470 Email: jmeschke@u.washington.edu.

Filter ExampleFilter Example

Water coming from Water coming from sedimentation sedimentation basin.basin.

AnthraciteAnthracite

SandSand

Gravel (supportGravel (support

media)media)

Water going to disinfectionWater going to disinfection

Page 53: Water and wastewater treatment processes ENV H 452/ENV H 542 John Scott Meschke Office: Suite 2249, 4225 Roosevelt Phone: 206-221-5470 Email: jmeschke@u.washington.edu.

Mechanisms Involved in Filtration

Interception: hits & sticks

Sedimentation: quiescent, settles, & attaches

Flocculation: Floc gets larger within filter

Entrapment: large floc gets trapped in space between particles

Floc particles

Granular media, e.g., grain of sand

Removal of bacteria, viruses and protozoa by a granular media filter requires water to be coagulated

Page 54: Water and wastewater treatment processes ENV H 452/ENV H 542 John Scott Meschke Office: Suite 2249, 4225 Roosevelt Phone: 206-221-5470 Email: jmeschke@u.washington.edu.

Rapid filtration

• To remove particulates in water• Flow rate: 2-4 gpm/ft2

• Turbidity: < 0.5 NTU (often times < 0.1 NTU)• Reduction of microbes

– 50-98 % Total coliform – 50-98 % of fecal coliform – 10-99 % of enteric viruses– 97-99.9 % of Giardia– 99 % of Cryptosporidium

Page 55: Water and wastewater treatment processes ENV H 452/ENV H 542 John Scott Meschke Office: Suite 2249, 4225 Roosevelt Phone: 206-221-5470 Email: jmeschke@u.washington.edu.

Disinfection in water

• To inactivate pathogens in water

• Various types– Free chlorine– Chloramines– Chlorine dioxide– Ozone– UV

Page 56: Water and wastewater treatment processes ENV H 452/ENV H 542 John Scott Meschke Office: Suite 2249, 4225 Roosevelt Phone: 206-221-5470 Email: jmeschke@u.washington.edu.

Trend in disinfectant use (USA, % values)

Disinfectant 1978 1989 1999

Chlorine gas 91 87 83.8

NaClO2 (bulk) 6 7.1 18.3

NaClO2 (on-site)

0 0 2

Chlorine dioxide

0 4.5 8.1

Ozone 0 0.4 6.6

Chloramines 0 20 28.4

Page 57: Water and wastewater treatment processes ENV H 452/ENV H 542 John Scott Meschke Office: Suite 2249, 4225 Roosevelt Phone: 206-221-5470 Email: jmeschke@u.washington.edu.

Comparison of major disinfectants

Consideration Disinfect ants

Cl2 ClO2 O3 NH2Cl

Oxidation potential

Strong Stronger? Strongest Weak

Residuals Yes No No Yes

Mode of action

Proteins/NA

Proteins/NA

Proteins/NA

Proteins

Disinfecting efficacy

Good Very good Excellent Moderate

By-products Yes Yes Yes? No