Concentration Polarization Quantification and Minimization in Cork Process Wastewater Ultrafiltration by an Ozone Pretreatment
| Autor: | Miguel Minhalma, Joaquin R. Dominguez, Maria Norberta De Pinho |
|---|---|
| Jazyk: | angličtina |
| Rok vydání: | 2021 |
| Předmět: |
Membrane fouling
Mass transfer coefficient membrane fouling Process Chemistry and Technology Chemical technology Intrinsic rejection coefficient Ultrafiltration Bioengineering mass transfer coefficient phenolic compounds TP1-1185 intrinsic rejection coefficient cork process wastewater Phenolic compounds ultrafiltration Chemistry Chemical Engineering (miscellaneous) Cork process wastewater QD1-999 |
| Zdroj: | Processes; Volume 9; Issue 12; Pages: 2182 Repositório Científico de Acesso Aberto de Portugal Repositório Científico de Acesso Aberto de Portugal (RCAAP) instacron:RCAAP Processes, Vol 9, Iss 2182, p 2182 (2021) |
| ISSN: | 2227-9717 |
| DOI: | 10.3390/pr9122182 |
| Popis: | Concentration polarization and membrane fouling have been identified as the main problems during the ultrafiltration treatment of cork processing wastewaters. These problems drastically reduce the permeate fluxes and, therefore, their potential applications. In this work, a soft ozonation pretreatment was applied to minimize these undesirable effects. A new systematic study was carried out for membranes with different molecular weight cut-offs and at different operating conditions to monitor and quantify the concentration polarization caused by the wastewater’s remaining ozonated compounds. Film theory was used to correlate the mass transfer coefficient, k, and the intrinsic rejection coefficient, f′, with the resistance introduced by concentration polarization. The ultrafiltration treatment was carried out under varying hydrodynamic operating conditions (circulating flow rates of 100–200 L/h) and transmembrane pressures (1–3 bar) for a set of four cellulose acetate membranes covering a wide range of molecular weight cut-offs (5000–100,000 Da) and hydraulic permeabilities (25–110 kg/h/m2/bar). The ozone pretreatment (at wastewater pH) reduced the phenolic content selectively (direct oxidation) by more than 50%, reducing membrane fouling and concentration polarization and increasing permeate fluxes (by 22–45%) and mass transfer coefficients (up to six times). |
| Databáze: | OpenAIRE |
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