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OVERVIEW OF THE FUTURE TRENDS IN WASTEWATER TREATMENT

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1 OVERVIEW OF THE FUTURE TRENDS IN WASTEWATER TREATMENT
Prof. Hallvard Ødegaard Department of Hydraulic and Environmental Engineering Norwegian University of Science and Technology (NTNU) N-7491 Trondheim – NORWAY NTNU - Norwegian University of Science and Technology Dep. Hydraulic and Environmental Engineering Prof. Hallvard Ødegaard

2 DEVELOPMENT OF WASTEWATER MANAGEMENT
NTNU - Norwegian University of Science and Technology Dep. Hydraulic and Environmental Engineering Prof. Hallvard Ødegaard

3 Prof. Hallvard Ødegaard
THE DEVELOPMENT OF WATER WITHDRAWAL IN THE WORLD WATER USE CHARACTERISTICS NTNU - Norwegian University of Science and Technology Dep. Hydraulic and Environmental Engineering Prof. Hallvard Ødegaard

4 MANY REGIONS IN DEVELOPING COUNTRIES ARE WITHOUT WASTEWATER TREATMENT
NTNU - Norwegian University of Science and Technology Dep. Hydraulic and Environmental Engineering Prof. Hallvard Ødegaard

5 Prof. Hallvard Ødegaard
THE MEGACITIES CHALLENGE Many megacities do not treat their wastewater or they treat by primary treatment only Mexico City Many of these cities are situated by the ocean They have little space for treatment plants They are in need for a affordable secondary treatment concept NTNU - Norwegian University of Science and Technology Dep. Hydraulic and Environmental Engineering Prof. Hallvard Ødegaard

6 EUTROPHICATION AND LACK OF NUTRIENT
REMOVAL IN MANY DEVELOPED COUNTRIES There is still a huge market for P- and N-removal in many developed countries: UK Eastern Europe US Japan Australia NTNU - Norwegian University of Science and Technology Dep. Hydraulic and Environmental Engineering Prof. Hallvard Ødegaard

7 Prof. Hallvard Ødegaard
REUSE OF THE TREATED WATER In most regions of the world the use of water has been : Supply driven Price of water low In the future water use in many regions will be : Demand driven Price of water will increase Extensive treatment of wastewater cost effective NTNU - Norwegian University of Science and Technology Dep. Hydraulic and Environmental Engineering Prof. Hallvard Ødegaard

8 RESOURCES IN WASTEWATER WILL HAVE TO
BE UTILISED Agricultural reuse - irrigation Urban reuse Industrial reuse Potable water reuse 1. The water itself 2. The constituents in the wastewater 3. The heat of the wastewater Nutrients (C,N,P) Carbon for energy production (biogas, biofuel) Metals for reuse (Al, Fe) Energy for heating/cooling NTNU - Norwegian University of Science and Technology Dep. Hydraulic and Environmental Engineering Prof. Hallvard Ødegaard

9 SELECTION OF FUTURE TREATMENT PROCESSES
MUST BE BASED ON WASTEWATER CHARACTERISTICS RECEIVING WATER CHARACTERISTICS TREATMENT EFFICIENCY COST SLUDGE PRODUCTION POTENTIAL USE OF UTILISING THE RESOURCES IN THE WASTEWATER NTNU - Norwegian University of Science and Technology Dep. Hydraulic and Environmental Engineering Prof. Hallvard Ødegaard

10 Prof. Hallvard Ødegaard
FACTORS THAT HAVE TO BE TAKEN INTO ACCOUNT TREATMENT EFFICIENCY Focus today : Oxygen consuming matter (BOD/COD and NH4-N) and nutrients (P and N) Focus in the future : Microbial contaminants (helminth eggs, parasitic protozoa, bacteria,virus ) Micropollutants (heavy metals as well as organic MPs) COST Cost is very much linked to space requirement – especially in the big cities Compact treatment alternatives will be asked for in many cases Biofilm systems may replace activated sludge systems High rate separation techniques may replace settling tanks SLUDGE PRODUCTION Disposal of sludge : Increasingly higher portion of total cost Methods are looked for that minimize sludge production and that utilize the resources of the sludge NTNU - Norwegian University of Science and Technology Dep. Hydraulic and Environmental Engineering Prof. Hallvard Ødegaard

11 Prof. Hallvard Ødegaard
NTNU - Norwegian University of Science and Technology Dep. Hydraulic and Environmental Engineering Prof. Hallvard Ødegaard

12 SUSTAINABLE WASTEWATER TREATMENT
STRATEGIES TOWARDS SUSTAINABLE WASTEWATER TREATMENT The role of particles NTNU - Norwegian University of Science and Technology Dep. Hydraulic and Environmental Engineering Prof. Hallvard Ødegaard

13 SIZE OF ORGANIC PARTICLES IN WASTEWATER
NTNU - Norwegian University of Science and Technology Dep. Hydraulic and Environmental Engineering Prof. Hallvard Ødegaard

14 CLASSIFICATION OF ORGANIC MATTER IN WASTEWATER ACCORDING TO SIZE
After Balmat (1957), Heukelekian and Balmat (1959), Richert and Hunter (1971) NTNU - Norwegian University of Science and Technology Dep. Hydraulic and Environmental Engineering Prof. Hallvard Ødegaard

15 Prof. Hallvard Ødegaard
EXAMPLES FROM SCANDINAVIAN WWT PLANTS Fraction of suspended COD and BOD NTNU - Norwegian University of Science and Technology Dep. Hydraulic and Environmental Engineering Prof. Hallvard Ødegaard

16 Prof. Hallvard Ødegaard
EXAMPLES FROM SCANDINAVIAN WWT PLANTS Fraction of N and P on suspended form Generally : Plants with high fraction of soluble COD has low fraction of particulate N and P assimilation in sewers NTNU - Norwegian University of Science and Technology Dep. Hydraulic and Environmental Engineering Prof. Hallvard Ødegaard

17 THE ASSOCIATION OF OTHER POLLUTANTS
TO PARTICLES Heavy metals (example from a wastewater treatment plant) Virus : 0,01 - 0,1 µm % adsorbed to particles Bacteria and 0, µm Parasitic protozoa : µm (Cryptospiridium: 4-6 µm) Helminth eggs : µm (Ascaris, Taenia) Organic micropollutants : Very high affinity to particles % of PCB and PAH associated to particles NTNU - Norwegian University of Science and Technology Dep. Hydraulic and Environmental Engineering Prof. Hallvard Ødegaard

18 SUMMARY ON CONSEQUENCE OF WASTEWATER CHARACTERISTICS
A very substantial reduction of all pollutants can very efficiently be removed by removing particles and colloids The rate at which proceeding biological processes will perform, will increase by removal of particles and colloids IT IS VERY LOGICAL TO ENHANCE PRIMARY TREATMENT for instance by pre-coagulation or by coarse filtration NTNU - Norwegian University of Science and Technology Dep. Hydraulic and Environmental Engineering Prof. Hallvard Ødegaard

19 MY BASIC WASTEWATER TREATMENT PHILOSOPHY :
Take out the particles first Then deal with the solubles Enhanced primary Removal of solubles Make use of the concentrate Carbon source Organic concentrate Biogas Utilize the resources from the concentrate Nutrients NTNU - Norwegian University of Science and Technology Dep. Hydraulic and Environmental Engineering Prof. Hallvard Ødegaard

20 Prof. Hallvard Ødegaard
WHAT IS ENHANCED PRIMARY TREATMENT ? TODAY Enhanced primary settling Cogulant aided Primary precipitation TOMORROW Coarse primary filtration Coagulant aided VERY SOON AFTER TOMORROW Membrane filtration NTNU - Norwegian University of Science and Technology Dep. Hydraulic and Environmental Engineering Prof. Hallvard Ødegaard

21 AVERAGE TREATMENT RESULTS IN NORWEGIAN PRIMARY PRECIPITATION PLANTS
NTNU - Norwegian University of Science and Technology Dep. Hydraulic and Environmental Engineering Prof. Hallvard Ødegaard

22 TRADITIONAL PRIMARY PRECIPITATION
DOWNSIDE OF TRADITIONAL PRIMARY PRECIPITATION LARGE SLUDGE PRODUCTION SP = SSin - SSout + Kprec * D SP = sludge production (g SS/m3) Kprec = sludge production coeff. (g SS/g Me)(Fe~4, Al~6) D = dose ofmetal coagulant (g Me/m3) NTNU - Norwegian University of Science and Technology Dep. Hydraulic and Environmental Engineering Prof. Hallvard Ødegaard

23 Prof. Hallvard Ødegaard
SLUDGE PRODUCTION CAN BE REDUCED BY USE OF POLYMER NTNU - Norwegian University of Science and Technology Dep. Hydraulic and Environmental Engineering Prof. Hallvard Ødegaard

24 Prof. Hallvard Ødegaard
ENHANCED PRIMARY TREATMENT BY COARSE MEDIA FILTRATION Pilot plant Plastic filter media L: light –polyethylene, 0,95 g/cm3 H: Heavy – PVC, 1,45 g/cm3 NTNU - Norwegian University of Science and Technology Dep. Hydraulic and Environmental Engineering Prof. Hallvard Ødegaard

25 ENHANCED PRIMARY TREATMENT
Comparison of single media filters: K1L and K2L filters NTNU - Norwegian University of Science and Technology Dep. Hydraulic and Environmental Engineering Prof. Hallvard Ødegaard

26 FAVORABLE COMBINATIONS
OF TREATMENT SYSTEMS NTNU - Norwegian University of Science and Technology Dep. Hydraulic and Environmental Engineering Prof. Hallvard Ødegaard

27 Prof. Hallvard Ødegaard
COMPACT SECONDARY TREATMENT ? You have taken out must of the particulate BOD and a relatively small amount of low MW, easily biodegradable, soluble BOD is left High-rate sedimentation Flotation Sand filtration Membrane filtration Residence time: 15–30 min min NTNU - Norwegian University of Science and Technology Dep. Hydraulic and Environmental Engineering Prof. Hallvard Ødegaard

28 Prof. Hallvard Ødegaard
THE PRINCIPLE OF THE MOVING BED REACTOR Aerobic reactor Anaerobic/anoxic reactor NTNU - Norwegian University of Science and Technology Dep. Hydraulic and Environmental Engineering Prof. Hallvard Ødegaard

29 THE KALDNES MOVING BED BIOFILM PROCESS
Aerated MBBR Carrier under water NTNU - Norwegian University of Science and Technology Dep. Hydraulic and Environmental Engineering Prof. Hallvard Ødegaard

30 SOLUBLE COD REMOVAL RATE VERSUS SOLUBLE COD LOADING RATE
Period 1 and 2 Period 3 NTNU - Norwegian University of Science and Technology Dep. Hydraulic and Environmental Engineering Prof. Hallvard Ødegaard

31 “OBTAINABLE” COD REMOVAL RATE VERSUS
TOTAL COD LOADING RATE ”Obtainable" COD removal rate : (CODinfluent-SCODeffluent)*Q/A Period 1 and 2 Period 3 NTNU - Norwegian University of Science and Technology Dep. Hydraulic and Environmental Engineering Prof. Hallvard Ødegaard

32 RESULTS SETTLING EXPERIMENTS
Influence of organic loading rate in bioreactor on settleability Influence of polymer addition on settleability Medium charge, high MW cationic polymer NTNU - Norwegian University of Science and Technology Dep. Hydraulic and Environmental Engineering Prof. Hallvard Ødegaard

33 SECONDARY TREATMENT PROCESS
A HIGH RATE SECONDARY TREATMENT PROCESS NTNU - Norwegian University of Science and Technology Dep. Hydraulic and Environmental Engineering Prof. Hallvard Ødegaard

34 SSEFFL VERSUS ME-DOSE AND POLYMER DOSE
PolyDADMAC NTNU - Norwegian University of Science and Technology Dep. Hydraulic and Environmental Engineering Prof. Hallvard Ødegaard

35 PARTICULATE COD FRACTIONS IN RAW AND FLOTATED WATER
WITH DIFFERENT POLYDADMAC DOSAGES AND 0.2 MMOL FE/L . NTNU - Norwegian University of Science and Technology Dep. Hydraulic and Environmental Engineering Prof. Hallvard Ødegaard

36 LAMELLA FLOTATION UNIT
HIGH RATE FLOTATION UNITS LAMELLA FLOTATION UNIT 20-25 m/h NTNU - Norwegian University of Science and Technology Dep. Hydraulic and Environmental Engineering Prof. Hallvard Ødegaard

37 MEMBRANE BIOREACTORS FOR WW TREATMENT
Membrane bioreactors are being taken into use, mainly based on low-loaded activated sludge systems Activated sludge membrane bioreactors has the ability to overcome the inherent weaknesses of AS (large volume, poor settling) But there are still many challenges: Energy consumption Pre-treatment Cost Membrane biofilm reactors will be developed that may have higher fluxes, less cake formation and simpler membrane cleaning NTNU - Norwegian University of Science and Technology Dep. Hydraulic and Environmental Engineering Prof. Hallvard Ødegaard

38 NEW TYPES OF MEMBRANES AND MEMBRANE MODULES WILL BE DEVELOPED
Permeate Concentrate SEM of membrane: Feed Sintered metal membrane NTNU - Norwegian University of Science and Technology Dep. Hydraulic and Environmental Engineering Prof. Hallvard Ødegaard

39 Prof. Hallvard Ødegaard
WHAT ABOUT NITROGEN REMOVAL ? The principal nutrient removal strategies NTNU - Norwegian University of Science and Technology Dep. Hydraulic and Environmental Engineering Prof. Hallvard Ødegaard

40 CALCULATED BIODEGRADABLE, SOLUBLE COD
(BSCOD) CONCENTRATION VS TOTAL COD IN SOME SCANDINAVIAN PLANTS NTNU - Norwegian University of Science and Technology Dep. Hydraulic and Environmental Engineering Prof. Hallvard Ødegaard

41 PROCESSES TAKING PLACE
IN THE SEWER SYSTEM NTNU - Norwegian University of Science and Technology Dep. Hydraulic and Environmental Engineering Prof. Hallvard Ødegaard

42 Prof. Hallvard Ødegaard
GARDERMOEN WWTP (Bioreactor HRT: 3 hrs) NTNU - Norwegian University of Science and Technology Dep. Hydraulic and Environmental Engineering Prof. Hallvard Ødegaard

43 PRE-COAGULATION/COMBINED DENITRIFICATION
WITH INTERNALLY MADE CARBON SOURCE PRODUCED FROM SLUDGE BY THERMAL HYDROLYSIS NTNU - Norwegian University of Science and Technology Dep. Hydraulic and Environmental Engineering Prof. Hallvard Ødegaard

44 Prof. Hallvard Ødegaard
Cost/benefit analyses for different methods NTNU - Norwegian University of Science and Technology Dep. Hydraulic and Environmental Engineering Prof. Hallvard Ødegaard

45 Prof. Hallvard Ødegaard
Energy/benefit evaluation for different methods NTNU - Norwegian University of Science and Technology Dep. Hydraulic and Environmental Engineering Prof. Hallvard Ødegaard

46 Prof. Hallvard Ødegaard
SUSTAINABLE URBAN WATER SYSTEMS Two schools : 1. The present centralized system should be replaced by alternative systems based on local handling 2. The present centralized system is the only realistic one, but it should be modified to be in agree- ment with sustainable development NTNU - Norwegian University of Science and Technology Dep. Hydraulic and Environmental Engineering Prof. Hallvard Ødegaard

47 IN SMALL DECENTRALISED CYCLES
SOURCE SEPARATION IN SMALL DECENTRALISED CYCLES New equipment may be needed Example: Urine-separating toilets NTNU - Norwegian University of Science and Technology Dep. Hydraulic and Environmental Engineering Prof. Hallvard Ødegaard

48 NATURE-BASED (low-tech) PROCESS-BASED (high-tech)
HIGH-TECH OR LOW-TECH LOCAL WWTP SOLUTIONS ? NATURE-BASED (low-tech) SOLUTIONS PROCESS-BASED (high-tech) SOLUTIONS NTNU - Norwegian University of Science and Technology Dep. Hydraulic and Environmental Engineering Prof. Hallvard Ødegaard

49 Prof. Hallvard Ødegaard
NATURE-BASED (LOW-TECH) Ponds Contructed wetlands Infiltration systems CONSTRUCTED WETLAND FILTER NTNU - Norwegian University of Science and Technology Dep. Hydraulic and Environmental Engineering Prof. Hallvard Ødegaard

50 Prof. Hallvard Ødegaard
PROCESS-BASED (HIGH-TECH) SYSTEMS Japanese Johkasou Norwegian SBR-plant NTNU - Norwegian University of Science and Technology Dep. Hydraulic and Environmental Engineering Prof. Hallvard Ødegaard

51 Prof. Hallvard Ødegaard
RECLAIMED WASTEWATER FOR URBAN REUSE Reclaimed wastewater for toilet flushing in dual systems Reclaimed wastewater for landscaping (lakes, brooks, wetlands) Two approaches: citywide system small scale local systems Great demand for acceptable water Extraction from potable water source too expensive-not sustainable NTNU - Norwegian University of Science and Technology Dep. Hydraulic and Environmental Engineering Prof. Hallvard Ødegaard

52 THE TWO OUTGOING STREAMS FROM A WASTEWATER TREATMENT PLANT
The wastewater Water itself Nutrients Heat The wastewater sludge Nutrients Energy potential Biogas and Biofuel Metals (coagulants) NTNU - Norwegian University of Science and Technology Dep. Hydraulic and Environmental Engineering Prof. Hallvard Ødegaard

53 Prof. Hallvard Ødegaard
FINAL SLUDGE DISPOSAL OPTIONS DEPOSITION/CONTAINMENT On land – landfills – phasing out In the ocean – phased out Incineration ash deposition RECYCLING (”PRODUCTIFICATION”) Production of ”bio-soils” Recovery of phosphate Recovery of energy USE ON LAND Direct use on farmland as fertilizer/soil conditioner Use of ”bio-solis” (constructed soils) on green areas Quantity and disposal of communal sludge in EU (in 1000 tons of dry solids) NTNU - Norwegian University of Science and Technology Dep. Hydraulic and Environmental Engineering Prof. Hallvard Ødegaard

54 USE OF “BIO-SOILS” ON “GREENS”
THE ”USE ON LAND” STRATEGIES DIRECT USE ON FARMLAND USE OF “BIO-SOILS” ON “GREENS” The most commonly used and probably the most sustainable sludge resource recycling option ! But : Under considerable threat ! Bio-soils: Mixture of treated sludge, filling materials (sand, clay, bark etc) and nutrients (N,P,K) Primarily used on green areas (parks, sporting fields, gardens, green houses) NTNU - Norwegian University of Science and Technology Dep. Hydraulic and Environmental Engineering Prof. Hallvard Ødegaard

55 Prof. Hallvard Ødegaard
TREATMENT REQUIREMENTS FOR DIRECT USE ON LAND HYGIENIZATION – to prevent infection of people and animals STABILISATION – to prevent odour DEWATERING – to ease the spreading of sludge on farmland NTNU - Norwegian University of Science and Technology Dep. Hydraulic and Environmental Engineering Prof. Hallvard Ødegaard

56 Prof. Hallvard Ødegaard
RECYCLE/PRODUCTIFICATION STRATEGIES The market place Internal loops Sludge ”factory” Local recycling Centralized recycling NTNU - Norwegian University of Science and Technology Dep. Hydraulic and Environmental Engineering Prof. Hallvard Ødegaard

57 THE MARKET POTENTIAL OF THE PRODUCTS
THE MARKET POTENTIAL OF THE PRODUCTS Only bio-soils, electricity, phosphate and heat seem to have a potential NTNU - Norwegian University of Science and Technology Dep. Hydraulic and Environmental Engineering Prof. Hallvard Ødegaard

58 Prof. Hallvard Ødegaard
EXAMPLES FROM USE OF ”BIO-SOILS” IN TRONDHEIM Graveyard Topsoil Ski-jump Turfroof Gardens NTNU - Norwegian University of Science and Technology Dep. Hydraulic and Environmental Engineering Prof. Hallvard Ødegaard

59 Prof. Hallvard Ødegaard
ENERGY MANAGEMENT AT RYA District heating Treated water 6-7oC colder Heat power engine for el-production Boiler for heat product. Biogas for car-fuel Treated waste water Heat pump plant Gas storage Waste water sludge Bio-soil Biogas plant w/heat exchanger NTNU - Norwegian University of Science and Technology Dep. Hydraulic and Environmental Engineering Prof. Hallvard Ødegaard

60 Prof. Hallvard Ødegaard
Heat from incineration Heat value of raw sludge : 14 MJ/kgDS (3,85 kWh/kgDS) ----”---- digested sludge : 12 MJ/kgDS (3,30 kWh/kgDS) The biogas potential should be taken out before incineration The energy needed for evaporation of the water is balanced by the energy produced by incineration at a sludge DS of about 25 %. Higher DS gives a net heat amount Typical process solutions : Dewat. Drying Inciner. Hydrol. Dewat. Inciner. Hydrol. Digest. Dewat. Inciner. Dewat. Drying. Bio-Pellets NTNU - Norwegian University of Science and Technology Dep. Hydraulic and Environmental Engineering Prof. Hallvard Ødegaard

61 EXAMPLE OF A SLUDGE PRODUCT RECYCLING CONCEPT
(KREPRO) Recyclable products: Biofuel Precipitant Phosphorous Carbon source for N-removal Removed : Pathogens Heavy metals NTNU - Norwegian University of Science and Technology Dep. Hydraulic and Environmental Engineering Prof. Hallvard Ødegaard

62 UTILIZING SLUDGE IN BUILDING PRODUCTS
(here: cement production in Jaoan) NTNU - Norwegian University of Science and Technology Dep. Hydraulic and Environmental Engineering Prof. Hallvard Ødegaard

63 Prof. Hallvard Ødegaard
CONCLUSIONS I believe that we will see a change in technologies towards: Wastewater as a resource This requires special attention to : The role of particles Appropriate selection of processes Recycling of nutrients (P) Hygienic control Adapted from Du Pont PERMASEP Permeators NTNU - Norwegian University of Science and Technology Dep. Hydraulic and Environmental Engineering Prof. Hallvard Ødegaard


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