Hydrodynamic and Performance Evaluation of a Porous Ceramic Membrane Module Used on the Water–Oil Separation Process: An Investigation by CFD
Autor: | Guilherme Luiz de Oliveira Neto, Ricardo Soares Gomez, Severino Rodrigues de Farias Neto, Nívea Gomes Nascimento de Oliveira, João M.P.Q. Delgado, Lucas Pereira Castanheira Nascimento, Paloma Lima de Oliveira, Antonio Gilson Barbosa de Lima, Hortência Luma Fernandes Magalhães |
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Jazyk: | angličtina |
Rok vydání: | 2021 |
Předmět: |
separation
Materials science Membrane permeability Separator (oil production) Filtration and Separation 02 engineering and technology lcsh:Chemical technology Article Membrane technology law.invention 020401 chemical engineering law Ansys Fluent Chemical Engineering (miscellaneous) lcsh:TP1-1185 lcsh:Chemical engineering 0204 chemical engineering Filtration Process Chemistry and Technology lcsh:TP155-156 021001 nanoscience & nanotechnology Produced water Volumetric flow rate Membrane Ceramic membrane Chemical engineering membranes produced water 0210 nano-technology CFD |
Zdroj: | Membranes Volume 11 Issue 2 Membranes, Vol 11, Iss 121, p 121 (2021) |
ISSN: | 2077-0375 |
DOI: | 10.3390/membranes11020121 |
Popis: | Wastewater from the oil industry can be considered a dangerous contaminant for the environment and needs to be treated before disposal or re-use. Currently, membrane separation is one of the most used technologies for the treatment of produced water. Therefore, the present work aims to study the process of separating oily water in a module equipped with a ceramic membrane, based on the Eulerian–Eulerian approach and the Shear-Stress Transport (SST k-ω) turbulence model, using the Ansys Fluent® 15.0. The hydrodynamic behavior of the water/oil mixture in the filtration module was evaluated under different conditions of the mass flow rate of the fluid mixture and oil concentration at the entrance, the diameter of the oil particles, and membrane permeability and porosity. It was found that an increase in the feed mass flow rate from 0.5 to 1.5 kg/s significantly influenced transmembrane pressure, that varied from 33.00 to 221.32 kPa. Besides, it was observed that the particle diameter and porosity of the membranes did not influence the performance of the filtration module it was also verified that increasing the permeability of the membranes, from 3 × 10−15 to 3 × 10−13 m2, caused transmembrane pressure reduction of 22.77%. The greater the average oil concentration at the permeate (from 0.021 to 0.037 kg/m3) and concentrate (from 1.00 to 1.154 kg/m3) outlets, the higher the average flow rate of oil at the permeate outlets. These results showed that the filter separator has good potential for water/oil separation. |
Databáze: | OpenAIRE |
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