Selecting model for treatmentof oily wastewater by MF-PAC hybrid process using mullite-alumina ceramic membranes
Hermia’s models for cross flow filtration were used to investigate the fouling mechanisms of mullite-alumina ceramic membranes in treatment of oily wastewaters in a hybrid microfiltration-powdered activated carbon process (MF-PAC). Results show that cake filtration model can be applied for predictio...
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| Дата: | 2016 |
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| Автори: | , |
| Формат: | Стаття |
| Мова: | English |
| Опубліковано: |
Інститут колоїдної хімії та хімії води ім. А.В. Думанського НАН України
2016
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| Назва видання: | Химия и технология воды |
| Теми: | |
| Онлайн доступ: | http://dspace.nbuv.gov.ua/handle/123456789/160801 |
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| Назва журналу: | Digital Library of Periodicals of National Academy of Sciences of Ukraine |
| Цитувати: | Selecting model for treatmentof oily wastewater by MF-PAC hybrid process using mullite-alumina ceramic membranes / Mohsen Abbasi, Aboozar Taheri // Химия и технология воды. — 2016. — Т. 38, № 3. — С. 311-323. — Бібліогр.: 18 назв. — рос. |
Репозитарії
Digital Library of Periodicals of National Academy of Sciences of Ukraine| id |
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irk-123456789-1608012019-11-21T01:26:10Z Selecting model for treatmentof oily wastewater by MF-PAC hybrid process using mullite-alumina ceramic membranes Mohsen Abbasi Aboozar Taheri Технология водоподготовки и деминерализация вод Hermia’s models for cross flow filtration were used to investigate the fouling mechanisms of mullite-alumina ceramic membranes in treatment of oily wastewaters in a hybrid microfiltration-powdered activated carbon process (MF-PAC). Results show that cake filtration model can be applied for prediction of permeation flux decline for MF and MF-PAC process up to 400 ppm PAC. The complete pore blocking model and the intermediate pore blocking model can predict permeation flux decline with time for MF-PAC with 800 and 1200 ppm PAC respectively. Average error for prediction of permeation flux with cake filtration model is 2.19% for MF process and 2.16; 2.06 and 1.31% for MF-PAC process with 100; 200 and 400 ppm PAC respectively. Also for MF-PAC process with 800 and 1200 ppm PAC, average error for prediction of permeation flux with complete pore blocking model and intermediate pore blocking model was 6.11 and 6% respectively. 2016 Article Selecting model for treatmentof oily wastewater by MF-PAC hybrid process using mullite-alumina ceramic membranes / Mohsen Abbasi, Aboozar Taheri // Химия и технология воды. — 2016. — Т. 38, № 3. — С. 311-323. — Бібліогр.: 18 назв. — рос. 0204-3556 http://dspace.nbuv.gov.ua/handle/123456789/160801 en Химия и технология воды Інститут колоїдної хімії та хімії води ім. А.В. Думанського НАН України |
| institution |
Digital Library of Periodicals of National Academy of Sciences of Ukraine |
| collection |
DSpace DC |
| language |
English |
| topic |
Технология водоподготовки и деминерализация вод Технология водоподготовки и деминерализация вод |
| spellingShingle |
Технология водоподготовки и деминерализация вод Технология водоподготовки и деминерализация вод Mohsen Abbasi Aboozar Taheri Selecting model for treatmentof oily wastewater by MF-PAC hybrid process using mullite-alumina ceramic membranes Химия и технология воды |
| description |
Hermia’s models for cross flow filtration were used to investigate the fouling mechanisms of mullite-alumina ceramic membranes in treatment of oily wastewaters in a hybrid microfiltration-powdered activated carbon process (MF-PAC). Results show that cake filtration model can be applied for prediction of permeation flux decline for MF and MF-PAC process up to 400 ppm PAC. The complete pore blocking model and the intermediate pore blocking model can predict permeation flux decline with time for MF-PAC with 800 and 1200 ppm PAC respectively. Average error for prediction of permeation flux with cake filtration model is 2.19% for MF process and 2.16; 2.06 and 1.31% for MF-PAC process with 100; 200 and 400 ppm PAC respectively. Also for MF-PAC process with 800 and 1200 ppm PAC, average error for prediction of permeation flux with complete pore blocking model and intermediate pore blocking model was 6.11 and 6% respectively. |
| format |
Article |
| author |
Mohsen Abbasi Aboozar Taheri |
| author_facet |
Mohsen Abbasi Aboozar Taheri |
| author_sort |
Mohsen Abbasi |
| title |
Selecting model for treatmentof oily wastewater by MF-PAC hybrid process using mullite-alumina ceramic membranes |
| title_short |
Selecting model for treatmentof oily wastewater by MF-PAC hybrid process using mullite-alumina ceramic membranes |
| title_full |
Selecting model for treatmentof oily wastewater by MF-PAC hybrid process using mullite-alumina ceramic membranes |
| title_fullStr |
Selecting model for treatmentof oily wastewater by MF-PAC hybrid process using mullite-alumina ceramic membranes |
| title_full_unstemmed |
Selecting model for treatmentof oily wastewater by MF-PAC hybrid process using mullite-alumina ceramic membranes |
| title_sort |
selecting model for treatmentof oily wastewater by mf-pac hybrid process using mullite-alumina ceramic membranes |
| publisher |
Інститут колоїдної хімії та хімії води ім. А.В. Думанського НАН України |
| publishDate |
2016 |
| topic_facet |
Технология водоподготовки и деминерализация вод |
| url |
http://dspace.nbuv.gov.ua/handle/123456789/160801 |
| citation_txt |
Selecting model for treatmentof oily wastewater by MF-PAC hybrid process using mullite-alumina ceramic membranes / Mohsen Abbasi, Aboozar Taheri // Химия и технология воды. — 2016. — Т. 38, № 3. — С. 311-323. — Бібліогр.: 18 назв. — рос. |
| series |
Химия и технология воды |
| work_keys_str_mv |
AT mohsenabbasi selectingmodelfortreatmentofoilywastewaterbymfpachybridprocessusingmullitealuminaceramicmembranes AT aboozartaheri selectingmodelfortreatmentofoilywastewaterbymfpachybridprocessusingmullitealuminaceramicmembranes |
| first_indexed |
2023-06-10T11:09:50Z |
| last_indexed |
2023-06-10T11:09:50Z |
| _version_ |
1796154618484359168 |