Title: ESM 214 05
1ESM 214 05
- Lecture 5 / 6 Physical Chemical Processes in
Waste Treatment
2Physical Chemical Processes
- May precede Biological Treatment
- e.g. flow equalization
- e.g. preliminary and primary treatment
- May contribute to Biological Treatment
- e.g. precipitation in secondary clarifier
- e.g. aeration
- May follow Biological Treatment
- e.g. advanced treatment
3Concept of Flow Equalization
- Dampen out diurnal fluctuations
- Divert toxics
- Balance loads
High flow diversion
Low flow return
Qi
Qi
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5Some physical and chemical processes used with
biological treatment are for combining
- -- mixing flocculation
- -- aeration
6Often the purpose of, physical and chemical
processes is to separate
- -- solids from liquid
- -- dissolved chemicals from liquid
- -- gases from liquid
7Separating Solids
- Settling
- Discrete particles
- Flocculants
- Precipitants
- Flotation
- Filtration
- Granular media
- Membrane
- Centrifugation
8Discrete Particle Settling
- Modeled by Stokes law (p 363 ME)
- Spherical, homogeneous particles
- No flocculation
- Vc depth? (Q / V) Q/A overflow rate
- Only particles with velocity gt Vc are removed
- Grit removal 30 sec to a few minutes
- Primary sedimentation (clarification) 1000
g/sf-d
9Example Primary clarification
- Circular or rectangular basins
- 1.5 to 2.5 hour detention time
- Significant removal of BOD (up to 45)
- Removal of TSS (up to 70)
- Fractionation of VSS from TSS
10Flocculation
- Flocculation formation of aggregates that settle
- Can occur during settling
- May be helped by coagulants
11Flocs in activated sludge.
12Coagulants / Precipitants
Alum Al2(SO4)318H2O Aluminum chloride
AlCl3 Lime Ca(OH)2 Ferric chloride
FeCl3 Ferric sulfate Fe2(SO4)3 Ferrous
sulfate FeSO4 7H2O Sodium aluminate Na2Al2O4
13Dissolved Air Flotation Thickner (DAFT)
14Depth vs Surface Filtration
15Granular filter filtration cycle
16Granular filter backwash cycle
17Granular filter variables
- Influent and effluent quality
- Filter media (size, shape, etc.)
- Filter bed (depth, mixing, porosity,
stratification) - Filtration flow rate
- Chemicals
- Headloss allowed
- Backwashing
18Membrane filtration process
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21Membrane processes by mechanism
- Hydrostatic pressure ?
- Microfiltration (MF) 0.08 2.0 mm
- Ultrafiltration (UF) 0.005 0.2 mm
- Nanofiltration (NF) 0.001- 0.01 mm
- Reverse Osmosis (RO) 0.0001 0.001 mm
- Diffusion across a concentration ?
- Dialysis (2 to 50 nm pore size)
- Electromotive force
- Electrodialysis ( less than 2 nm)
22Sieving (top) as in MF and UF Ion
rejection (bottom) as in NF and RO
23Osmosis
24Reverse Osmosis
25Separating Dissolved Chemicals from Liquids
- Membrane filtration (as before)
- Adsorption
- Ion Exchange
26Adsorption
- Definition accumulation of substances at an
interface (e.g. solid / liquid) - Adsorbate substance being transferred
- Adsorbent recipient interface
- Activated carbon may be used in WWT
- Char from organics
- Activation develops pores (1 nm to 25 nm)
- GAC and PAC
27Sorption onto activated carbon
28Activated carbon plug flow reactor.
29Ion Exchange
- See Fig. 11-77 in text. (pg. 1195)
- Ions in solution displace and replace ions on
exchange substrate - e.g. Ca and Mg replacing Na
- zeolites (aluminosilicates)
- NH4 and NO3- can be removed
- Cationic and anionic resins for TDS removal
- Heavy metal (e.g. Cd, Zn, Ni, Cu) removal
30ion exchange schematic
31Gas Stripping
- Moves gas from liquid phase into gas phase and
away - Contact liquid with clean air
- Ammonia, VOCs, odorous gases
- Continuous or intermittent flow
- Counter-, Co- or Cross-current flow regimes
32Counter current stripping tower for VOC removal.
33Ammonia stripping
NH4 ? NH3 H
34Advanced Treatmentmay include
- Filtration for solids removal
- RO for dissolved organics and inorganics
- Adsorption (e.g. GAC) for organics
- Air Stripping for volatile organics and ammonia
- Ion exchange for dissolved ions, TDS