二次改性高渗反渗透膜在矿井水脱盐处理中的应用及技术经济性分析

Technical and economic analysis of reverse osmosis membrane with high permeability via post-treatment method in treating mine water

  • 摘要: 煤矿矿井水是重要的非常规水资源,矿井水的分级处理与分质利用对缓解矿区水资源紧张和生态环境保护具有重要意义。反渗透脱盐技术因其技术成熟、工艺稳定等优势已在高矿化度矿井水处理工程中广泛应用。然而,反渗透技术脱盐能耗随处理料液含盐量浓度提升而大幅攀升,且产水水质总溶解固体含量(TDS)远低于地表III类水硫酸盐及氯化物限值(低于250 mg/L),此举不仅造成能源浪费,更易引发浓水排放压力倍增、膜污染加剧等衍生问题。基于此,面向矿井水实际脱盐需求,提出一种高渗反渗透膜的二次改性策略,并探究其技术‒经济可行性。首先以自配水作为原水,以脱盐率适度下降及渗透性大幅提升为目标,对反渗透平板膜片进行化学改性,通过膜性能及表征量化指标确定出最优的化学接触时间为9 h。之后,基于膜片试验结果,对4040膜元件进行化学改性试验,并在自配水及实际矿井水体系下验证改性策略的适用性,结果表明:由平板膜得到的在线浸泡氯解条件可适用于卷式膜的在线氯解处理,且在实际矿井水为原水的168 h长期试验中,膜通量提升幅度可达40%,脱盐率持续稳定在98%以上。最后,通过试验结果构建经济成本评估模型,证实了基于脱盐适度下降且高渗反渗透膜的脱盐系统可实现矿井水低耗化处理。以1000 m3/d产水量,回收率15%为例,在保证产水量一致的情况下,装配改性膜可将原操作压力由1 MPa下降至0.755 MPa,吨水能耗下降0.12 kWh/m3,可有效涵盖二次化学改性的费用支出。因此,该研究旨在探索出适用于煤矿矿井水绿色分质处理的脱盐率适度下降且高渗反渗透的改性策略,为高矿化度矿井水脱盐工艺的开发提供新的研究思路。

     

    Abstract: The mine water in coal mines is an important unconventional water resource. The hierarchical treatment and quality-specific utilization of mine water are of great significance for alleviating the shortage of water resources in mining areas and protecting the ecological environment. Reverse osmosis desalination technology has been widely applied in the treatment projects of high-mineralization mine water due to its advantages such as mature technology and stable process. However, the desalination energy consumption of reverse osmosis technology increases significantly with the rise in the salt concentration of the treated feed liquid. Moreover, the total dissolved solids (TDS) content of the produced water is far lower than the limits of sulfate and chloride in Class III surface water (below 250 mg/L). This not only causes energy waste but also more easily triggers derivative problems such as a significant increase in the pressure of concentrated water discharge and aggravated membrane pollution. Based on this, a secondary modification strategy of moderately desalinated high-permeability reverse osmosis membranes is proposed for the actual desalination demand of mine water, and explores its technical-economic feasibility. Firstly, using self-prepared water as the raw water and aiming at a moderate decrease in desalination rate and a significant increase in permeability, the reverse osmosis flat membrane is chemically modified, and the optimal chemical contact time is determined to be 9 hours through membrane performance and quantified characterization indicators. Afterwards, based on the membrane test results, a chemical modification test is carried out on the 4040 membrane element, and the applicability of the modification strategy is verified under the self-prepared water and actual mine water systems. The results show that the online soaking chlorination conditions obtained from the flat membrane can be applied to the online chlorination treatment of the spiral wound membrane, and in the 168-hour long-term test with actual mine water as the raw water, the increase range of the membrane flux can reach up to 40% and the desalination rate remains continuously stable above 98%. Finally, by constructing an economic cost assessment model through the test results, it is confirmed that the desalination system based on the moderately desalinated high-permeability reverse osmosis membrane can realize the low-consumption treatment of mine water. Taking a daily production of 1000 m3 and a recovery rate of 15% as an example, under the condition of ensuring the same water production, assembling the modified membrane can reduce the original operating pressure from 1 to 0.755 MPa, and the energy consumption per ton of water decreases by 0.12 kWh/m3, which can effectively cover the expense of the secondary chemical modification. Therefore, the research aims to explore a moderately desalinated high-permeability reverse osmosis modification strategy suitable for the green fractionated treatment of coal mine water, and provide a new research idea for the development of the desalination process of highly mineralized mine water.

     

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