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Achieving Low Mercury Concentrations In Chlor-Alkali Wastewaters

机译:在氯碱废水中实现低汞浓度

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In the early 1980's EPA established production-based effluent limitation guidelines for mercury in wastewater discharges from mercury cell chlor-alkali plants based on the application of best available technology economically achievable (BAT). The principal process for achieving the BAT guidelines has been chemical precipitation with sulfide compounds followed by filtration to remove the mercury as insoluble mercury sulfide. This treatment process typically results in effluent mercury concentrations ranging from 10 to 50 ppb. In response to changes in environmental laws in Maine in 1997, HoltraChem Manufacturing Company in Orrington, Maine began searching for new technologies for reducing mercury in its effluent. Working with suppliers, an on-site pilot plant test with sulfur-impregnated, activated carbon, MERSORB? LW mercury adsorbent, indicated that achieving effluent mercury levels of < 100 ppt was feasible. A full-scale treatment system was designed and installed after the existing primary sulfide treatment process to treat 100 gpm of wastewater. Mercury concentrations after initial start-up of the secondary adsorption process were one to two orders of magnitude higher than expected. After optimization of the sulfide treatment process, optimizing pH of the influent and the addition of 0.5 micron filters prior to the adsorption trains, mercury concentrations averaging < 100 ppt and as low as 20 ppt have been achieved.
机译:在20世纪80年代初的EPA中,基于在经济上可实现的技术(BAT)的最佳技术的应用,从汞细胞氯碱植物中建立了基于生产的废水汞的汞限制指南。实现BAT指南的主要方法是用硫化物化合物的化学沉淀,然后过滤以除去汞作为不溶性汞硫化物。该处理过程通常导致排出汞浓度为10-50ppb。为了应对1997年缅因州环境法的变化,缅因州霍尔特拉罕的制造公司开始寻找新技术,以减少流出物中的汞。与供应商一起使用,现场试验厂试验,硫磺浸渍,活性炭,MERSOLAL? LW汞吸附剂,表明达到了<100 ppt的污水水平是可行的。设计并安装了全尺寸的处理系统,在现有的硫化物处理过程中进行了一种,以治疗100GPm废水。次级吸附过程初始启动后的汞浓度是高于预期的一个至两个数量级。在优化硫化物处理过程后,在吸附列车之前优化流入的pH和加入0.5微米过滤器,达到了<100 ppt等20 ppt的汞浓度。

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