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中试规模的正向渗透处理脱硫废水的研究。

Pilot-scale study of forward osmosis for treating desulfurization wastewater.

机构信息

State Key Laboratory of Separation Membranes and Membrane Processes, School of Environmental Science and Engineering, Tiangong University, Tianjin 300387, China E-mail:

Fluid Technology Solutions (FTS), Inc., Beijing Office, Beijing 101101, China.

出版信息

Water Sci Technol. 2020 Dec;82(12):2857-2863. doi: 10.2166/wst.2020.533.

Abstract

Forward osmosis (FO) treatment of desulfurization wastewater shows great potential in laboratory scale tests. To explore the adaptability of the forward osmosis system in the practical treatment of desulfurization wastewater, we carried out a pilot test on desulfurization wastewater treated by the traditional method under the conditions of adding soda ash (SA) and adding FO scale inhibitor (FOSI). The results showed that the FO system could concentrate desulfurization wastewater with an average TDS of 15,816-32,820 mg/L in the influent water to an average TDS of more than 120,000 mg/L, which was concentrated 3.8-7.8 times. The removal rates of Ca, Mg and Cl were more than 99% and the system could operate stably for a long time. Under the condition of adding SA and FOSI, the system recovery rate was 85.38% and 73.02%, respectively. The operating cost was 25 RMB/ton and 21.77 RMB/ton, respectively. The results showed that the application of forward osmosis in desulfurization wastewater treatment was technically feasible and economically effective.

摘要

反渗透(FO)处理脱硫废水在实验室规模试验中显示出巨大的潜力。为了探索反渗透系统在实际脱硫废水处理中的适应性,我们在添加纯碱(SA)和添加 FO 阻垢剂(FOSI)的条件下,对传统方法处理的脱硫废水进行了中试试验。结果表明,FO 系统可以将进水 TDS 平均为 15816-32820mg/L 的脱硫废水浓缩至 TDS 平均超过 120000mg/L,浓缩倍数为 3.8-7.8 倍。Ca、Mg 和 Cl 的去除率均大于 99%,系统可以长时间稳定运行。在添加 SA 和 FOSI 的条件下,系统回收率分别为 85.38%和 73.02%。运行成本分别为 25 元/吨和 21.77 元/吨。结果表明,反渗透在脱硫废水处理中的应用在技术上是可行的,在经济上是有效的。

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