State Key Laboratory of Urban Water Resource and Environment, School of Environment, Harbin Institute of Technology, Harbin 150090, China E-mail:
Water Sci Technol. 2020 Jun;81(12):2674-2684. doi: 10.2166/wst.2020.331.
Coal chemical industry (CCI) generally utilizes reverse osmosis (RO) for water reclamation, which generates a highly concentrated stream containing refractory organic substances and high-concentration total dissolved solids (TDS). To address this issue, the present work focuses on volume reduction of RO concentrate (ROC) produced from CCI by forward osmosis (FO). We investigated the effects of membrane orientation and draw solution (DS) concentration on FO performance. Foulant removal was tested by using chemical cleaning, physical cleaning and osmotic backwash (OB). AL-FS (active layer facing feed solution) mode outcompeted AL-DS (active layer facing draw solution) mode, achieving a flux of 26.4 LMH, 92.5% water reclamation and energy consumption of 0.050 kWh·m with 4 M NaCl as DS. The FO process was able to reject >98% SO , Mgand Ca, 92-98% Si and 33-55% total organic carbon (TOC). Ten-cycle (10 × 20 h) accelerated fouling test demonstrated approximately 30% flux decline in association with Si-containing foulants, which could be removed almost completely through OB with 97.1% flux recovery. This study provides a proof-of-concept demonstration of FO for volume reduction and water reclamation of ROC produced from CCI, making the treatment of ROC more efficient and more energy effective.
煤化工(CCI)通常采用反渗透(RO)进行水回收,这会产生含有难处理有机物和高浓度总溶解固体(TDS)的高度浓缩流。针对这一问题,本工作重点研究了采用正向渗透(FO)对 CCI 产生的 RO 浓缩液(ROC)进行体积减少的方法。我们考察了膜朝向和汲取液(DS)浓度对 FO 性能的影响。采用化学清洗、物理清洗和反渗透冲洗(OB)对污染物去除效果进行了测试。活性层朝向进料溶液(AL-FS)模式优于活性层朝向汲取溶液(AL-DS)模式,采用 4 M NaCl 作为 DS 时,FO 通量达到 26.4 LMH,水回收率为 92.5%,能耗为 0.050 kWh·m。FO 过程能够去除 >98%的 SO 、Mg 和 Ca、92-98%的 Si 和 33-55%的总有机碳(TOC)。10 个循环(10×20 h)加速结垢测试表明,与含 Si 污染物相关的通量下降约 30%,通过 OB 可以几乎完全去除,通量恢复率达到 97.1%。本研究为 FO 用于减少 CCI 产生的 ROC 的体积和水回收提供了概念验证,使 ROC 的处理更加高效和节能。