The performance of settling tanks depends on several interrelated processes and factors that include: hydrodynamics, settling, turbulence, sludge rheology, flocculation, temperature changes and heat exchange, geometry, loading, the nature of the floc, the atmospheric conditions and the total dissolved solids concentration. A Quasi-3D (Q3D) clarifier model has been developed to include the following factors: axisymmetric hydrodynamics (including the swirl component), five types of settling (nonsettleable particles, unflocculated discrete settling, flocculated discrete settling, hindered settling and compression), turbulence, sludge rheology, flocculation with four classes of particles, temperature changes and surface heat exchange with the atmosphere, various external and internal geometry configurations, unsteady solids and hydraulic loading, the nature of the floc settling/interaction. The model includes: shear flocculation, differential settling flocculation and sweep flocculation. The Q3D model reproduces the major features of the hydrodynamic processes and solids distribution on secondary clarifiers. When the model is executed with the field derived settling characteristics, it can accurately predict the effluent and recirculation suspended solids concentrations. The model has been formulated to conserve fluid, tracer and solids mass. The model has been developed and tested using field data from the UNO Pilot Plant and the Jefferson Parish Waste Water Treatment Plant located at Marrero, Louisiana. A field testing procedure is presented that addressees all of the settling regimes that are encountered in a Secondary Settling Tank. Results obtained with the Q3D model indicate that the flocculation process plays a major role in the effluent suspended solids (ESS) on secondary clarifiers. The extent of actual flocculation depends on the design of the center well and on the concentration of the incoming mixed liquor suspended solids (MLSS). The center well promotes flocculation, but its most important benefit is the improvement on the tank hydrodynamics. The changes in temperature on secondary clarifiers play an important role on the performance of secondary settling tanks. The gravity induced radial velocities in the sludge blanket are higher than the radial velocities of the scraper in the region near the hopper, therefore the blades are not highly effective in conveying the solids in this region.

Abstract Flocculation plays a critical role in the activated sludge process, where flocs are removed by settling and where unsatisfactory flocculation is resulting in poor effluent quality. Control and operation of the process is also challenging as it is sensitive to external and internal disturbances. Furthermore, stricter environmental demands are also being placed on wastewater treatment and discharge quality thus solutions are needed to improve the current systems. A novel optical monitoring method employing a tube flow and a CCD camera was developed to characterize the flocs and filaments of the sludge, and the method was tested on samples from full-scale activated sludge plants. An online device operating on the same principle was also developed and this was tested over a period of eight months at municipal wastewater treatment plant. Optical monitoring was employed in the laboratory to study the breakage of activated sludge flocs. Based on the image analysis data, in the industrial plant the major breakage process was large-scale fragmentation. In the two municipal plants, it was surface erosion. The flocs had more filaments and were more irregular in shape in the industrial plant, which could be the reason for the large-scale fragmentation. The effect of floc morphology on the effluent clarity of the activated sludge process was studied in the industrial and municipal activated sludge plants by optical monitoring over periods of three months and eight months, respectively. The changes in floc morphology took place slowly in both plants. Four major factors that correlated with the purification results were the size and shape of the flocs and the quantities of small particles and filaments. The image analysis results suggested that the settling problem that occurred during the test periods in the industrial plant was caused by dispersed growth, whereas that in the municipal plant was caused by filamentous bulking. In conclusion, it is possible to use the developed method online in order to analyse the state of flocculation. Thus the method could be useful when developing online monitoring applications for quantifying floc characteristics and for diagnosing the causes of settling problems in the wastewater treatment plants. / Tiivistelmä Aktiivilieteprosessissa flokkulaatiolla on merkittävä rooli, sillä muodostuneet flokit poistetaan prosessista laskeutuksen avulla. Siten huono flokkulaatio johtaa puhdistetun jäteveden kiintoainemäärän lisääntymiseen. Prosessin säätö ja operointi on kuitenkin hankalaa, sillä aktiivilieteprosessi on herkkä ulkoisille ja sisäisille häiriöille. Jätevedenpuhdistukseen liittyvät ympäristövaatimukset ja päästöehdot vesistöihin ovat myös tiukentuneet, joten uusia menetelmiä tarvitaan parantamaan nykyisiä prosesseja. Tässä työssä kehitettiin uusi, optinen kuvantamismenetelmä karakterisoimaan flokkeja ja rihmoja. Menetelmä hyödyntää putkivirtausta ja CCD-kameraa ja sitä testattiin aktiivilietelaitosten näytteillä. Lisäksi kehitettiin samaa periaatetta noudattava online-laitteisto, jota testattiin kahdeksan kuukauden ajan. Optista kuvantamista testattiin laboratoriossa flokkien hajoamistutkimuksessa. Kuva-analyysitulosten perusteella kahden kunnallisen aktiivilietelaitoksen flokit hajosivat pintaeroosioon perustuvan mallin mukaan ja teollisen aktiivilietelaitoksen flokit hajosivat fragmentaatiomallin mukaan. Teollisen aktiivilietelaitoksen flokeissa oli enemmän rihmoja ja ne olivat epäsäännöllisemmän muotoisia, mikä voi olla syynä flokkien fragmentaatioon. Flokkien morfologian vaikutus jäteveden puhdistustuloksiin tutkittiin teollisessa (kolmen kuukauden ajan) ja kunnallisessa (kahdeksan kuukauden ajan) aktiivilietelaitoksessa optisella kuvantamismenetelmällä. Molemmissa laitoksessa muutokset flokkien morfologiassa tapahtuivat hitaasti. Neljä tärkeintä tekijää, jotka korreloivat puhdistustulosten kanssa, olivat flokkien koko ja muoto sekä pienten partikkelien ja rihmojen määrä. Kuva-analyysitulosten perusteella laskeutumisongelma teollisessa jätevesilaitoksessa johtui flokinmuodostajabakteerien liian pienestä määrästä ja kunnallisessa jätevesilaitoksessa rihmamaisten bakteerien liikakasvusta. Yhteenvetona voidaan todeta, että kehitettyä menetelmää on mahdollista käyttää online-mittarina sekä sen avulla voidaan arvioida flokkulaation tilannetta. Siten menetelmää on mahdollista hyödyntää flokkien ominaisuuksien karakterisoinnissa ja arvioidessa jätevedenkäsittelylaitoksen laskeutumisongelmien aiheuttajaa.