BioE 411 and AE/CE/BRT 511
Wastewater treatment
Attached growth systems: sewage farms
Morestead sewage farm
Berlin sewage farm layout
Sewage farm
Overland flow designs
Improved attached growth:
early biobed
Large-scale wastewater treatment
Rotating disc arrangement
Simple treatment: septic tank
Leach field after septic tank
Suspended growth systems
So far, we have studied systems where treatment is
effected by bacteria, and other organisms, which are
attached to a solid medium, i.e. soil, rocks, etc.
There are also systems where the microbial growth
occurs in suspension. The bacteria then aggregate
into flocs, which are barely visible to the naked eye,
but each consists of millions of bacteria and often
protozoa attached to the floc.
Systems range from the simple facultative lagoon or pond, with no
aeration, to aerated ponds and to sophisticated activated sludge systems,
where the biomass is separated from the effluent and recycled to treatment
and excess production treated separately.
The simple lagoon or pond systems purify the water quite well, but since
there is no provision to separate the biomass production, the effluent is
quite turbid and still contains much organic material, but stabilized to a
non-smelling and not rapidly degrading form.
Facultative lagoons
Facultative lagoons or stabilization ponds use only natural phenomena and
almost no mechanical action. Oxygenation for bacterial oxidation of
organics comes from photosynthesis by algae and a bit from wind.
CO2 released by bacteria is used by the algae. Excess biomass and other
settleables are treated by anaerobic bacteria at the bottom.
Facultative lagoon interactions
http://www2.bren.ucsb.edu/~keller/courses/esm223/esm223_15.pdf
Design approaches to pond
treatment systems
Ponds usually require lengthy treatment periods, weeks for facultative
systems and days for aerated systems. Although facultative systems have
very little mixing other than inflow, gas bubbles and wind effects, the long
retention periods ensures some homogeneity except with respect to depth, as
there is much stratification.
As in any mixed system, the contents have the same concentration as the
overflow. This means that the organisms in the pond continuously experience
a low level of substrate to feed on, which slows down the treatment
considerably, as the typical first-order reactions are directly proportional to the
BOD. Therefore, significant improvement in treatment rate can be achieved
by approaching a channel (tube) flow, or using multiple ponds.
Multiple pond system analysis can be performed by assuming that each is a
completely mixed system, operating on a first-order degradation and a mass
balance around each provides one equation. Intermediate values can be
eliminated as of no interest, so the solution will provide final effluent quality for
given retention times, or more importantly, retention times to achieve a
necessary effluent quality.
Activated sludge process
Activated sludge flocs
Note filamentous bacteria
Note Vorticella and
other protozoa
Activated sludge model
L
L0
L
L
L
L
Activated sludge plants
Hyperion, Playa del Rey, CA)
Primary aeration tank
Oxygenated systems
Cryogenic air separation facility, Hyperion, Playa del Rey, CA)
Settling tanks
Secondary settling tank, Hyperion, Playa del Rey, CA)
Aerobic suspended systems –
activated sludge
Volumetric loading = QL0/V
QL0
Nitrogen removal
 Nitrification (Nitrosomonas and Nitrobacter)
NH3 + O2  NO2
-  NO3
-
 Denitrification
NO3
- + organics  CO2 + N2
 Process adaptations
Anoxic Aerobic
Air
Phosphate removal
 BNR plants
 Discarding phosphate anaerobically
 Luxury aerobic uptake of P in aerobic stage
 Process adaptations for N and P removal
Anaerobic Anoxic Aerobic
Air
Wastewater
Excess biomass disposal
 Production
 Separation
 Further biological treatment – (an)aerobic
 Dewatering
 Drying – solar or gas heated
 Disposal/ beneficial use – soil amender/fertilizer
or fuel
The cost of biomass disposal amount to about half the cost
of wastewater treatment. Aeration, if used, almost up to
half of the rest of the cost. If no aeration, the capital cost ,
including the cost of land, could be very high.
Typical steps in modern wastewater treatment
How are living beings classified?
Linnaeus
(1735)
2 kingdoms
Haeckel
(1866)
3 kingdoms
Chatton
(1925)
2 groups
Copeland
(1938)
4 kingdoms
Whittaker
(1969)
5 kingdoms
Woese
(1977,1990)
3 domains
Animalia Animalia
Eukaryote
Animalia Animalia
Eukarya
Vegetabilia Plantae
Plantae Plantae
Protoctista
Fungi
Protista
(not
treated)
Protista
Procaryote Monera Monera
Archaea
Bacteria
Historic development of classification
How are living beings classified?
Two super-
.kingdoms
Three domains Six kingdoms
Mineralia non-life
Biota/
Vitae
life
Acytota / Aphanobionta
(Viruses, Viroids, Prions?, ...)
non-cellular life
Cytota
cellular life
Prokaryota
/ Procarya
(Monera)
Bacteria Eubacteria
Archaea Archaebacteria
Eukaryota / Eucarya
Protista
Fungi
Plantae
Animalia
Carl Woese’s Tree of Life

WASTEWATER TREATMENT plant for architecure

  • 1.
    BioE 411 andAE/CE/BRT 511 Wastewater treatment
  • 2.
  • 3.
  • 4.
  • 5.
  • 6.
  • 7.
  • 8.
  • 9.
  • 10.
  • 11.
    Leach field afterseptic tank
  • 12.
    Suspended growth systems Sofar, we have studied systems where treatment is effected by bacteria, and other organisms, which are attached to a solid medium, i.e. soil, rocks, etc. There are also systems where the microbial growth occurs in suspension. The bacteria then aggregate into flocs, which are barely visible to the naked eye, but each consists of millions of bacteria and often protozoa attached to the floc. Systems range from the simple facultative lagoon or pond, with no aeration, to aerated ponds and to sophisticated activated sludge systems, where the biomass is separated from the effluent and recycled to treatment and excess production treated separately. The simple lagoon or pond systems purify the water quite well, but since there is no provision to separate the biomass production, the effluent is quite turbid and still contains much organic material, but stabilized to a non-smelling and not rapidly degrading form.
  • 13.
    Facultative lagoons Facultative lagoonsor stabilization ponds use only natural phenomena and almost no mechanical action. Oxygenation for bacterial oxidation of organics comes from photosynthesis by algae and a bit from wind. CO2 released by bacteria is used by the algae. Excess biomass and other settleables are treated by anaerobic bacteria at the bottom.
  • 14.
  • 15.
    Design approaches topond treatment systems Ponds usually require lengthy treatment periods, weeks for facultative systems and days for aerated systems. Although facultative systems have very little mixing other than inflow, gas bubbles and wind effects, the long retention periods ensures some homogeneity except with respect to depth, as there is much stratification. As in any mixed system, the contents have the same concentration as the overflow. This means that the organisms in the pond continuously experience a low level of substrate to feed on, which slows down the treatment considerably, as the typical first-order reactions are directly proportional to the BOD. Therefore, significant improvement in treatment rate can be achieved by approaching a channel (tube) flow, or using multiple ponds. Multiple pond system analysis can be performed by assuming that each is a completely mixed system, operating on a first-order degradation and a mass balance around each provides one equation. Intermediate values can be eliminated as of no interest, so the solution will provide final effluent quality for given retention times, or more importantly, retention times to achieve a necessary effluent quality.
  • 16.
  • 17.
    Activated sludge flocs Notefilamentous bacteria Note Vorticella and other protozoa
  • 18.
  • 19.
  • 20.
  • 21.
    Oxygenated systems Cryogenic airseparation facility, Hyperion, Playa del Rey, CA)
  • 22.
    Settling tanks Secondary settlingtank, Hyperion, Playa del Rey, CA)
  • 23.
    Aerobic suspended systems– activated sludge Volumetric loading = QL0/V QL0
  • 24.
    Nitrogen removal  Nitrification(Nitrosomonas and Nitrobacter) NH3 + O2  NO2 -  NO3 -  Denitrification NO3 - + organics  CO2 + N2  Process adaptations Anoxic Aerobic Air
  • 25.
    Phosphate removal  BNRplants  Discarding phosphate anaerobically  Luxury aerobic uptake of P in aerobic stage  Process adaptations for N and P removal Anaerobic Anoxic Aerobic Air Wastewater
  • 26.
    Excess biomass disposal Production  Separation  Further biological treatment – (an)aerobic  Dewatering  Drying – solar or gas heated  Disposal/ beneficial use – soil amender/fertilizer or fuel The cost of biomass disposal amount to about half the cost of wastewater treatment. Aeration, if used, almost up to half of the rest of the cost. If no aeration, the capital cost , including the cost of land, could be very high.
  • 27.
    Typical steps inmodern wastewater treatment
  • 28.
    How are livingbeings classified? Linnaeus (1735) 2 kingdoms Haeckel (1866) 3 kingdoms Chatton (1925) 2 groups Copeland (1938) 4 kingdoms Whittaker (1969) 5 kingdoms Woese (1977,1990) 3 domains Animalia Animalia Eukaryote Animalia Animalia Eukarya Vegetabilia Plantae Plantae Plantae Protoctista Fungi Protista (not treated) Protista Procaryote Monera Monera Archaea Bacteria Historic development of classification
  • 29.
    How are livingbeings classified? Two super- .kingdoms Three domains Six kingdoms Mineralia non-life Biota/ Vitae life Acytota / Aphanobionta (Viruses, Viroids, Prions?, ...) non-cellular life Cytota cellular life Prokaryota / Procarya (Monera) Bacteria Eubacteria Archaea Archaebacteria Eukaryota / Eucarya Protista Fungi Plantae Animalia
  • 30.