Wastewater treatment
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Wastewater Treatment. On completion of this segment you should be:. Aware of the public health aspects and goals of wastewater treatment Able to describe the processes involved in primary, secondary and tertiary treatment

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Wastewater Treatment

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Wastewater treatment

Wastewater Treatment

On completion of this segment you should be:

  • Aware of the public health aspects and goals of wastewater treatment

  • Able to describe the processes involved in primary, secondary and tertiary treatment

  • Able to compare the differences between the fixed-film and suspended growth systems in biological treatment

  • Aware of some methods available for nutrient removal


Wastewater treatment goals

Wastewater Treatment Goals

  • Protect public health from contamination of water supplies

  • Reliable and economic operation

  • Minimum capital cost

Aims


Wastewater treatment goals cont

Wastewater Treatment Goals (cont)

  • Removal of floating, suspended and soluble matter

  • Reduce BOD, COD pathogenic organisms and nutrient

  • Maintain aesthetics of natural water bodies, ecology of water systems

Outcomes


Typical characteristics of wastewater

Typical Characteristics of Wastewater


Treatment selection

Treatment Selection

  • Wastewater treatment comprises primary, secondary and tertiary treatments

  • The selection of appropriate treatment processes is dependent upon the nature and strength of pollutants, quantity of flow, and discharge licence conditions


Primary treatment

Primary Treatment

  • Usually the first stage of wastewater treatment comprises largely physical processes.

  • A well-designed primary treatment should remove about 40 - 75% of TSS and about 25 - 40% BOD5

  • A possible pre-treatment is the injection of air, O2, H2O2 and pre-chlorination if the influent is 'stale’

  • Processes include screening, grit removal and primary settling


Screens

Screens

The removal of large objects that may damage pumps or block channels

  • Fixed or mechanical

  • Velocity in channels about 0.3 - 0.4 m/s

  • Design for PWWF

  • All screenings to be removed/buried

  • Location of strong odour from decomposition


Mechanical bar screen

Mechanical bar screen


Rotating drum screen

Rotating drum screen


Comminutors

Comminutors

  • These are mechanical cutting screens that reduce the size of large objects

  • Shredded matter are returned to the flow stream

  • A by-pass may be included


Comminutor

Comminutor


Grit chambers

Grit Chambers

  • Purpose is to remove inorganic grit/sand 0.2 - 1 mm size through differential settling

  • Aim is to prevent damage to pumps, blockage of channels and cementing of sludge in settling tanks

  • Two types of grit chambers, namely constantly velocity and aerated/spiral flow tanks


Constant velocity grit chamber

Constant Velocity Grit Chamber

  • Class I settling - horizontal flow

  • Uniform velocity at 0.25 - 0.35 m/s

  • Ideal parabolic shape or approximation

  • Width:depth ratio 1:1

  • Length  18 x max. depth


Constant velocity grit chamber1

Constant Velocity Grit Chamber


Aerated or spiral flow grit chamber

Aerated or Spiral Flow Grit Chamber

  • Flexibility of control; more efficient grit removal and can assist pre-aeration

  • Air supply or spiral flow controls the amount of silt removed

  • Suitable for larger population > 10 000 ep

  • HRT of about 3 min at PWWF


Aerated or spiral flow grit chamber1

Aerated or Spiral Flow Grit Chamber


Vortex flow grit chamber

Vortex Flow Grit Chamber


Primary sedimentation

Primary Sedimentation

Solids separation by gravity

  • Aim is to remove gross suspended solids (organic matter)

  • Largely class II settling of flocculent matter and natural coalescence or flocculation occurs

  • Surface skimmers remove floating matter (scum, grease etc)

  • The settled solids are pumped to an anaerobic digestion tank. The effluent (settled sewage) from primary treatment flows to the next stage ie. secondary treatment


Some features of primary settling

Some Features of Primary Settling

  • Design to accept 2 to 3 x ADWF

  • Removal of 40 - 75% suspended solids

  • Some incidental BOD5 reduction 25 - 40%

  • Hydraulic loading Q/A  30 m3/m2.d

  • Hydraulic retention time (HRT) 1.5 to 3 h; depth 2.5 to 5 m

  • Also act as flow/strength equalisation basins

  • Sludge scrapers should not cause re-suspension


Primary settling removed vs time

Primary settling % removed vs time


Types of primary settling tanks

Types of Primary Settling tanks

Rectangular horizontal-flow

  • Tanks use less space

  • Forward velocity 10 - 15 mm/s

  • Weir loading rate < 300 m3/m.d

  • Length:width ratio 3:1


Wastewater treatment

Rectangular horizontal-flow


Types of primary settling tanks1

Types of Primary Settling tanks

Up-flow tank

  • Square with 60o sludge hopper

  • No moving parts as sludge is removed hydrostatically

  • Some possible particle carry over


Wastewater treatment

Up-flow settling tank


Types of primary settling tanks2

Types of Primary Settling tanks

  • Inflow to a central stilling box

  • Radial-horizontal flow

  • Uses radial scrapers to remove sludge

Circular radial flow tank


Circular radial flow tank

Circular Radial Flow Tank


Circular radial flow tank1

Circular Radial Flow Tank


Circular radial flow tank2

Circular Radial Flow Tank


Pulteney bridge and weir city of bath

Pulteney Bridge and Weir, City of Bath


Secondary treatment

Secondary Treatment

Removal of dissolved solids through microbial action

  • Objective is to remove the remaining suspended solids and also dissolved solids

  • The process is mainly biological using microorganisms to convert the dissolved solids to biomass

  • Two distinct systems are available i.e. fixed film (trickling filter) and suspended growth (activated sludge)

  • The biomass is removed as sludge in final sedimentation tanks (clarifiers)


Typical microorganisms in activated sludge

Typical microorganisms in activated sludge


Fixed film systems

Fixed-Film Systems

  • Land treatment, trickling and rotating biological filters are predominantly aerobic biological processes

  • Land treatment ie. broadcasting of sewage, is one of the earliest forms of wastewater treatment


Trickling filter

Trickling Filter

  • Comprising an inert structure for growth of biofilm containing microorganisms (attached growth)

  • Microorganisms in biofilm interact with wastewater and metabolise the organic matter (BOD) into CO2 and H2O

  • Natural sloughing of the biofilm when it reaches a thickness that cannot be sustained

  • Filter medium voids (40 – 60%) promote air circulation and aerobic condition

  • Solids in the effluent are separated in the secondary settling (humus) tank


Interaction of biofilm

Interaction of biofilm


Trickling filter1

Trickling Filter


Trickling filters at wetalla

Trickling filters at Wetalla


A rotating biological contact unit

A rotating biological contact unit


Suspended growth systems

Suspended Growth Systems

  • Microorganisms are held in suspension as a high concentration flocculent, bulky matter through agitation, stirring

  • The microorganisms interact with influent wastewater and biodegrade organic matter into CO2, H2O and by-products, releasing energy for growth of new cells

  • The activated sludge process is an example of an aerobic suspended growth system. The anaerobic digester for the break down of waste sludge is an example of an anaerobic suspended growth system


Activated sludge process

Activated Sludge Process

  • The heart of the process is the reactor where aeration and oxidation of organic compounds occur

  • Microorganisms are held in suspension by aeration and stirring

  • Energy requiring process but has greater control and flexibility

  • Return activated sludge and sludge wasting maintain the design biomass concentration (MLVSS)

  • Final clarifier separates solids from the clear effluent and returns the settled sludge to the reactor


Activated sludge process with alternative wasting locations

Activated sludge process with alternative wasting locations


Surface aerators

Surface aerators


Final sedimentation tank

Final sedimentation tank


Final clarifier

Final clarifier


Comparison between attached film and suspended growth systems

Comparison between attached film and suspended growth systems


Wastewater disinfection

Wastewater Disinfection

  • Some microorganisms (105 – 107/100 mL) are still present in treated wastewater after secondary treatment

  • Disinfection is required to reduce pathogenic microorganisms

  • Chlorine is still the cost-effective disinfection, but requires minimum contact time and has adverse effects

  • Other environmental friendly methods include UVL, ozone disinfection, membrane microfiltration and constructed wetlands


Sludge digestion

Sludge Digestion

  • Sludge from primary and secondary settling tanks (including waste activated sludge) must be treated in digesters

  • Sludge is thickened before passing to sludge digesters

  • Sludge may be treated anaerobically or aerobically

  • Anaerobic sludge digestion involves 2 sequential stages ie. acid formation and methane formation

  • Digested sludge is dewatered before disposal


Low rate single stage sludge digester

Low rate single-stage sludge digester

.


High rate two stage sludge digester

High rate two-stage sludge digester

.


Anaerobic sludge digester

Anaerobic sludge digester

.


Aerobic sludge digester

Aerobic sludge digester

.


Tertiary treatment

Tertiary Treatment

  • Tertiary maturation ponds – an aerobic polishing process with detention time and further reduction in BOD and TSS (NFR)

  • Nutrient removal comprising nitrification and denitrification and phosphorus removal

  • Microfiltration and reverse osmosis


Wastewater treatment

Nano-membrane filtration


Nutrient removal

Nutrient Removal

The major components of nutrients in wastewater are nitrates and phosphates. They contribute to the eutrophication of receiving water

  • Total nitrogen may be about 35 mg/L and total phosphorus 8 mg/L after secondary treatment

  • Raw sewage composition of C:TN:TP  100:25:6

  • Normal plant growth only need C:TN:TP of 100:15:1


Nitrogen removal

Nitrogen Removal

Involves two stages of microbial action under different conditions

  • Ammonia is first oxidised to nitrites and nitrates through a process of nitrification by microorganisms

  • Nitrification uses aerobic autotrophic microorganisms

  • Dinitrification uses facultative heterotrophic microorganisms under anoxic condition where nitrates are converted to nitrogen gas


Phosphorus removal

Phosphorus Removal

Process may be through chemical precipitation or by preferred microbial action

  • Use of coagulants e.g. lime, aluminium sulfate, ferric chlorine will precipitate phosphorus

  • Process is expensive and results in quantities of difficult sludge

  • Preferred process is through microbial action with uptake of phosphorus by a select group of microorganisms


Biological phosphorus removal

Biological phosphorus removal

Modified Bardenpho process


End of module 18

End of Module 18


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