A tubing TPPB (Two-Phase Partitioning Bioreactor) was operated with the objective of verifying the effectivetreatment of a phenolic syntheticwastewaterwith simultaneous polymeric tubing bioregeneration by introducingtubing effluent recycle and modifications to the Hydraulic Retention Time (HRT). 2,4-dichlorophenol (DCP)was employed as the target substrate and the bioreactorwas operated for a 3month period under severe loadingconditions (from77 to 384 mg/L d) with HRT in the tubing in the range of 2-4 h. Tubing effluent recycle (recycleflow rate/influent flow rate ratio= 0.3) was applied when a loss of performance was detected arising from theincreased load. For HRT values of 3 and 4 h, almost complete DCP removalwas achieved after a fewdays (1-5) ofoperationwhile for the 2 h HRT (i.e. in themost severe loading condition) the DCP removalwas >=97%. A beneficialeffect on the process performance arising from recycle application was evident for all the operating conditionsinvestigated, and was confirmed by statistical analysis. Essentially complete polymer bioregeneration wasachievedwhen the bioreactorwas operated at the lowest HRT (i.e. 2 h), combinedwith the application of tubingeffluent recycle. The results of this study highlighted several advantages of the tubing TPPB configuration in acomparative analysis of different regeneration options, including the possibility of operating continuously withsimultaneous bioregeneration and without the need for additional units or operational steps and extra-energyconsumption.
Self-regenerating polymeric tubing bioreactor for removal of toxic substrates: operational strategies to face long-term severe dynamic loading conditions
Tomei M. C.
;Mosca Angelucci D.;
2020
Abstract
A tubing TPPB (Two-Phase Partitioning Bioreactor) was operated with the objective of verifying the effectivetreatment of a phenolic syntheticwastewaterwith simultaneous polymeric tubing bioregeneration by introducingtubing effluent recycle and modifications to the Hydraulic Retention Time (HRT). 2,4-dichlorophenol (DCP)was employed as the target substrate and the bioreactorwas operated for a 3month period under severe loadingconditions (from77 to 384 mg/L d) with HRT in the tubing in the range of 2-4 h. Tubing effluent recycle (recycleflow rate/influent flow rate ratio= 0.3) was applied when a loss of performance was detected arising from theincreased load. For HRT values of 3 and 4 h, almost complete DCP removalwas achieved after a fewdays (1-5) ofoperationwhile for the 2 h HRT (i.e. in themost severe loading condition) the DCP removalwas >=97%. A beneficialeffect on the process performance arising from recycle application was evident for all the operating conditionsinvestigated, and was confirmed by statistical analysis. Essentially complete polymer bioregeneration wasachievedwhen the bioreactorwas operated at the lowest HRT (i.e. 2 h), combinedwith the application of tubingeffluent recycle. The results of this study highlighted several advantages of the tubing TPPB configuration in acomparative analysis of different regeneration options, including the possibility of operating continuously withsimultaneous bioregeneration and without the need for additional units or operational steps and extra-energyconsumption.File | Dimensione | Formato | |
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