Title: Outline Water/Wastewater Treatment (Chapter 8)
1OutlineWater/Wastewater Treatment (Chapter 8)
- Overview
- Removal of solids (Chapter 8.6)
- ? Removal of hardness in water (Chapter 8.7)
- Kill of pathogenic bacteria (Chapter 8.11)
- Removal of dissolved inorganics (Chapter 8.8)
- Removal of nutrients (N P) (Chapter 8.8)
- Removal of dissolved organics (Chapter 8.9)
- Treatment disposal of sludge (Chapter 8.10)
2An Overview Water / Wastewater Treatment
- Similarity between Water Treatment and Wastewater
Treatment - Both require solids removal and disinfection
- Difference between Water Treatment and Wastewater
Treatment - Purpose Drinking water vs. sewage
- Unit process and operation w/ and w/o biological
process - Regulation SDWA vs. NPDES
3Types of Water / Wastewater Treatment
MethodsCommon classification (for wastewater)
(p. 232 - 237)
- Primary treatment
- Purpose To remove settable and floatable solids
- Method screening, grit removal, primary
sedimentation - Secondary treatment
- Purpose To aerobically and biologically remove
biodegradable organic matter - Method activated sludge, trickling filter,
rotating biological contactors - Tertiary (advanced) treatment
- Purpose To further remove SS, dissolved organics
(refractory compounds) and inorganics (N, P
nutrients) - Method activated carbon, nitrification /
denitrification
4Types of Water / Wastewater Treatment Methods
- Based on contaminants to be removed (detailed in
handout) - Suspended solids sedimentation,
coagulation/flocculation, filter - Biodegradable organics activated sludge,
trickling filter - Volatile organics air stripping, carbon
adsorption - Pathogens disinfection (Cl2, O3, UV)
- Nutrients (N) nitrification/denitrification, NH3
stripping (p.252) - Nutrients (P) precipitation, biological removal,
adsorption (Al2O3) - Refractory organics carbon adsorption, O3/UV
radiation - Hardness (Ca2, Mg2), heavy metals
precipitation, ion exchange, membrane processes,
chelation (sequestion) - Grease flotation, biological processes
- Dissolved solids ion exchange, membrane processes
5Water / Wastewater Treatment Selected Topics
- Removal of suspended solids
- Coagulation / Flocculation
- Removal of hardness
- Water Softening
- Removal of pathogenic bacteria
- Disinfection
6Typical Water Treatment Plant (Chapter 8.2)
Primary Settling
Coagulation/ Flocculation
Secondary Settling
Surface Water
Filtration
Disinfection
Clean water to consumer
Sludge
Sludge
Primary Settling
Coagulation/ Flocculation
Secondary Settling
Filtration
Disinfection
Aeration
Ground Water
Clean water to consumer
Sludge
Sludge
Well
7Typical Wastewater Treatment Plant (Chapter 8.4)
Bar Screen Grit Removal
Primary Settling
Aeration (Biological)
Secondary Settling
Disinfection
Effluent discharged to receiving water
Wastewater
Return Sludge (Bacteria)
Sludge Thickening
Sludge Stabilization
Waste Sludge
Sludge Dewatering
Dewatered sludge to landfill
Supernatant
8Topic I. Removal of Solids (Chapter 8.6)
- Solids in water and wastewater
- Dead animals, plant biomass, food debris
- Soil particles (clay, sand, etc.)
- Colloidal particles (humic substances)
- Bacterial cells, algal cells, virus
- Sludge
- Primary methods for the removal of solids
- Screening physical process
- Filtration physical process
- Settling physicochemical processes including
coagulation and flocculation
9Coagulation for the Removal of SolidsWhat? Why?
How? (p. 132 p.238-239)
- What? Coagulation involves the reduction of
electrostatic repulsion such that colloidal
particles of identical materials may aggregate. - Why? Colloidal particles are prevented from
aggregating by electrostatic repulsion of the
electrical double layers. They are small in size
and very stable in water. - How? By the addition of coagulants followed by
flocculation (p. 132)
10Common Coagulants
- Alum
- Hydrated aluminum sulfate Al2(SO4)318H2O
- Alum, when added to water, will be hydrolyzed to
form gelatinous hydroxide Al(OH)3 precipitate.
This will carry suspended solids as it settles by
gravity. - Anhydrous Fe3
- Forms Fe(OH)3 (s) in a wide range of pH 4-11
- Anhydrous Fe2 (copperas, FeSO47H2O)
- Must be oxidized to Fe3 first at pH higher than
8.5 - Natural and synthetic polyelectrolytes
- Starch, cellulose derivatives, proteinaceous
materials, and gums composed of polysaccharides - Synthetic polymers
11ExampleWater Treatment for Solids Removal
- Suspended solids are to be removed through
coagulation / flocculation followed by gravity
settling. Alum and lime are added at
stoichiometric rates sufficient to form 25 mg/L
of aluminum hydroxide sludge. For the following
data, calculate the alum and lime dosage, the dry
weight mass of solids generated per day, and the
wet volume per day of sludge. - Given data
- Flow 1.0 MGD
- TSS 5.0 mg/L
- Thickened sludge 20,000 mg/L
- Given reaction
- Al2(SO4)3 3Ca(OH)2 ? 2Al(OH)3 ? 3CaSO4
12Topic II. Removal of Hardness (Ca2, Mg2)Water
Softening
- Hardness is an important water quality parameter
in determining the suitability of water for
domestic and industrial uses - Hard waters require considerable amounts of soap
to produce foam - Hard waters produce scale in hot-water pipers,
heaters and boilers - Ca2 2HCO3- ? CaCO3 (s) CO2 (g) H2O
- Groundwater is generally harder than surface
water - Principal cations causing hardness and the major
anions associated with them (in decreasing order
of abundance in natural waters) - Cations Ca2, Mg2, Sr2, Fe2, Mn2
- Anions HCO3-, SO42-, Cl-, NO3-, SiO32-
13Water Hardness
- Hardness expressed in mg/L as CaCO3
- Methods of determination
- Calculation (see example)
- Hardness (mg/L) as CaCO3 M2 (mg/L) x 50 / EW
of M2 - EDTA titrimetric method
- M2 Eriochrome Black T (blue) ? (M
Eriochrome Black T)complex (wine red) - Water softening is needed when hardness is above
150-200 mg/L Hardness 50-80 is acceptable in
treated water
14Carbonate and Noncarbonate Hardness
- Total hardness Carbonate hardness
Noncarbonate hardness - Carbonate hardness temporary hardness
eliminated at elevated temperatures in boilers - Ca2 2HCO3- ? CaCO3 CO2 H2O
- Ca2 2HCO3- Ca(OH)2 ? 2CaCO3 2H2O
- Noncarbonate hardness permanent hardness can
not be removed or precipitated by boiling.
Noncarbonate hardness cations are associated with
SO42-, Cl- and NO3-.
15Example Harness Calculation
- Calculate the hardness of a water sample with the
following analysis
16Water Softening Methods (p. 240-244)
- Ion exchange
- Reverse osmosis
- Coagulation /flocculation (most commonly used)
- Ca2, Mg2 ? CaCO3 (s), Mg(OH)2 (s)
- lime-only process when Ca2 is present primarily
as bicarbonate hardness - lime-soda Ca(OH)2-Na2CO3 process when
bicarbonate is not present at substantial level
17Lime-Soda Ca(OH)2-Na2CO3 Process for Water
Softening Chemical Reactions Involved
- Lime to remove Ca2 in the form of natural
alkalinity - Ca(HCO3)2 Ca(OH)2 ? 2CaCO3? 2H2O
- Lime to remove Mg2 in the form of natural
alkalinity - Mg(HCO3)2 Ca(OH)2 ? MgCO3 (soluble) CaCO3?
2H2O - additional lime must be added to remove MgCO3
- MgCO3 Ca(OH)2 ? CaCO3? Mg(OH)2?
- Mg2 hardness in the form of a sulfate requires
both lime and soda ash - MgSO4 Ca(OH)2 ? CaSO4 Mg(OH)2?
- CaSO4 Na2CO3 ? CaCO3? Na2SO4?
- CO2 in the water will also consume lime
- CO2 Ca(OH)2 ? CaCO3 ? H2O
18Lime-Soda Ca(OH)2-Na2CO3 Process
Recarbonation by bubbling CO2 after softening
- Recarbonation is usually required after lime-soda
process - Why?
- To prevent super-saturated CaCO3 (s) and Mg(OH)2
(s) from forming harmful deposits or undesirable
cloudiness in water at a later time - CaCO3 (s) CO2 H2O ? Ca2 2HCO3-
- MgCO3 (s) CO2 H2O ? Ca2 2HCO3-
- To neutralize excessively high pH caused by
Na2CO3 - OH- CO2 ? HCO3-
19Topic III. Disinfection Kill of Pathogenic
Bacteria in Water
- Disinfection is typically the last step in a
water / wastewater treatment system - Residual chlorine is needed in distribution
system after water / wastewater treatment - In addition to disinfection, chlorine also has
the following functions - taste and odor control as an oxidizing agent
- oxidation of Fe2 and Mn2 in groundwater
- ammonium removal in domestic waste treatment
- slime, biofouling control control of sludge
bulking
20Types of Disinfection
- Gaseous Cl2
- Most commonly used
- Advantage provide residual chlorine for the
protection from bacterial growth in distribution
system - Disadvantage The formation of disinfection
by-products (trihalomethanes) presents a health
risk - Chlorine dioxide (ClO2)
- No disinfection by-products such as
trihalomethanes - Ca(ClO)2
- Safer than Cl2
- Ozone (p. 256-257)
- UV
21Chemistry of Chlorine in Water
- Cl2 H2O ? H Cl- HOCl
- HOCl is a weak acid with Ka 4.5x10-4 (HOCl
H OCl-) - HOCl and OCl- are free available chlorine which
are very effective in killing bacteria - Small amount of ammonium (NH4) in water is
desired - Chloramine NH2Cl, NHCl2, NCl3 (p. 255)
- Chloramines (combined available chlorine) are
weaker disinfectants than free available chlorine
but are desired residual chlorine to be retained
in water distribution system - Excessive amount of ammonium (NH4) in water is
undesirable because it consume excess demand of
Cl2 - Extra chlorine may be removed by SO2 , a process
called dechlorination - SO2 HOCl H2O ? Cl- SO42- 3H
22Example Chlorine Requirement
- Determine the quantity of chlorine gas (lb/day)
that must be supplied for breakpoint chlorination
of municipal wastewater that contains 3 mg/L of
ammonia-nitrogen. The wastewater flow rate is 1.0
MGD (Mgal/day). The relevant reactions are
provided below - Cl2 H2O ? HCl HOCl
- 2NH3 3HOCl ? N2 3H2O 3HCl
23Other Methods Removal of Dissolved Inorganics
Organics
- Inorganics
- Distillation
- Membrane process
- Electrodialysis
- Ion exchange
- Reverse osmosis
- Filtration
- Nanofiltration
- Ultrafiltration
- Microfiltration
- Organics
- Adsorption
- Activated carbon (AC)
- PAC (powered)
- GAC (granulated)
- Synthetic polymer
- XAD
- Oxidation
- O3
- H2O2
- O2
24Other Methods Removal of Nutrients
- Nitrogen (p. 251-252)
- Air stripping NH3
- Nitrification followed by denitrification
- NH4 ion exchange
- Biosynthesis
- Chlorination
- Phosphorus (p. 249-251)
- Biological uptake
- activated sludge
- Precipitation (Table 8.1)
- Adsorption
- Activated alumina, Al2O3