A Sequential Membrane Process of Ultrafiltration Forward Osmosis and Reverse Osmosis for Poultry Slaughterhouse Wastewater Treatment and Reuse

被引:10
作者
Fatima, Faryal [1 ]
Du, Hongbo [1 ]
Kommalapati, Raghava R. [1 ,2 ]
机构
[1] Prairie View A&M Univ, Ctr Energy & Environm Sustainabil, Prairie View, TX 77446 USA
[2] Prairie View A&M Univ, Dept Civil & Environm Engn, Prairie View, TX 77446 USA
基金
美国国家科学基金会; 美国食品与农业研究所;
关键词
poultry slaughterhouse wastewater; ultrafiltration; reverse osmosis; chemical oxygen demand; total phosphorous; total solids; total volatile solids; total fixed solids; total nitrogen;
D O I
10.3390/membranes13030296
中图分类号
Q5 [生物化学]; Q7 [分子生物学];
学科分类号
071010 ; 081704 ;
摘要
To address some challenges of food security and sustainability of the poultry processing industry, a sequential membrane process of ultrafiltration (UF), forward osmosis (FO), and reverse osmosis (RO) is proposed to treat semi-processed poultry slaughterhouse wastewater (PSWW) and water recovery. The pretreatment of PSWW with UF removed 36.7% of chemical oxygen demand (COD), 38.9% of total phosphorous (TP), 24.7% of total solids (TS), 14.5% of total volatile solids (TVS), 27.3% of total fixed solids (TFS), and 12.1% of total nitrogen (TN). Then, the PSWW was treated with FO membrane in FO mode, pressure retarded osmosis (PRO) mode, and (L)-DOPA coated membrane in the PRO mode. The FO mode was optimal for PSWW treatment by achieving the highest average flux of 10.4 +/- 0.2 L/m(2)-h and the highest pollutant removal efficiency; 100% of COD, 100% of TP, 90.5% of TS, 85.3% of TVS, 92.1% of TFS, and 37.2% of TN. The performance of the FO membrane was entirely restored by flushing the membrane with 0.1% sodium dodecyl sulfate solution. RO significantly removed COD, TS, TVS, TFS, and TP. However, TN was reduced by only 62% because of the high ammonia concentration present in the draw solution. Overall, the sequential membrane process (UF-FO-RO) showed excellent performance by providing high rejection efficiency for pollutant removal and water recovery.
引用
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页数:18
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