摘要
It is rather difficult to separate high concentration of ammonium thiosulfate from ammonium thiocyanate in coking wastewater which results in resources waste and environment pollution. In this work, a membrane process of nanofiltration (NF) was applied to solve the problem. The experimental results showed that the NF membrane selectively retained (NH4)2S2O3 with a rejection of 95.0% at a concentration of more than 60gL-1. Meanwhile, the permeation of NH4SCN was 120.0% at a concentration of nearly 120gL-1. Diafiltration was optimized to ensure a high average salt rejection of 93.4% for (NH4)2S2O3. In addition, salt concentrations and yields can be predicted by theoretical calculation. The results reveal that the NF membranes are successful in separating high concentration of bi-component ammonium salt solutions into mono-component ones.
源语言 | 英语 |
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页(从-至) | 233-237 |
页数 | 5 |
期刊 | Desalination |
卷 | 268 |
期 | 1-3 |
DOI | |
出版状态 | 已出版 - 1 3月 2011 |