The performance of a biological aerated filter loaded with a novel non-sintered fly-ash ceramsite as pretreatment for dual membrane processes

This work focused on wastewater reclamation of secondary treated ethylene chemical plant effluent, which contained high conductivity and high organic concentration. To reduce the cost and improve operation stability, a biological aerated filter-ultrafiltration-reverse osmosis (BAF-UF-RO) process was...

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Veröffentlicht in:Environmental technology. - 1993. - 36(2015), 13-16 vom: 13. Juli, Seite 2024-34
1. Verfasser: Li, Lihua (VerfasserIn)
Weitere Verfasser: Hu, Chaowu, Dai, Xiulan, Jin, Wenjie, Hu, Cheng, Ma, Fang
Format: Online-Aufsatz
Sprache:English
Veröffentlicht: 2015
Zugriff auf das übergeordnete Werk:Environmental technology
Schlagworte:Journal Article Research Support, Non-U.S. Gov't biological aerated filter membrane fouling non-sintered fly-ash ceramsite reverse osmosis ultrafiltration Coal Ash Membranes, Artificial Soil Water Pollutants, Chemical
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245 1 4 |a The performance of a biological aerated filter loaded with a novel non-sintered fly-ash ceramsite as pretreatment for dual membrane processes 
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520 |a This work focused on wastewater reclamation of secondary treated ethylene chemical plant effluent, which contained high conductivity and high organic concentration. To reduce the cost and improve operation stability, a biological aerated filter-ultrafiltration-reverse osmosis (BAF-UF-RO) process was proposed. The feasibility and effectiveness of BAF loaded with a novel non-sintered fly-ash ceramsite (NSFC) as a pretreatment method of a dual membrane system were investigated in detail. The results showed that the CODCr, turbidity, NH3-N and the silt density index (SDI) in the effluent from the BAF were reduced to 24.2 mg/L, 12.17 NTU, 0.42 mg/L and 7.52, respectively, and most of the organic compounds were biodegraded. The BAF-UF-RO process was stable with a recovery rate of 75%, and the desalination rate was up to about 97.5%. Compared with the UF-RO process, the operating pressure and backwash frequency decreased from 1.12-1.26 Mpa and 3 times/d to 0.94-0.98 Mpa and 2 times/d, respectively. After continuous operation for four months, there appeared to be no need for chemical cleaning of the RO membrane. Moreover, the analysis results of X-ray photoelectron spectroscopy and Fourier transform infrared spectroscopy proved that there was only slight membrane fouling, which was mainly colloidal blocking caused by refractory organic compound 
650 4 |a Journal Article 
650 4 |a Research Support, Non-U.S. Gov't 
650 4 |a biological aerated filter 
650 4 |a membrane fouling 
650 4 |a non-sintered fly-ash ceramsite 
650 4 |a reverse osmosis 
650 4 |a ultrafiltration 
650 7 |a Coal Ash  |2 NLM 
650 7 |a Membranes, Artificial  |2 NLM 
650 7 |a Soil  |2 NLM 
650 7 |a Water Pollutants, Chemical  |2 NLM 
700 1 |a Hu, Chaowu  |e verfasserin  |4 aut 
700 1 |a Dai, Xiulan  |e verfasserin  |4 aut 
700 1 |a Jin, Wenjie  |e verfasserin  |4 aut 
700 1 |a Hu, Cheng  |e verfasserin  |4 aut 
700 1 |a Ma, Fang  |e verfasserin  |4 aut 
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773 1 8 |g volume:36  |g year:2015  |g number:13-16  |g day:13  |g month:07  |g pages:2024-34 
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