Department of Civil and Environmental Engineering, University of Illinois at Urbana-Champaign, Urbana, IL 61801, USA.
Department of Civil and Environmental Engineering, University of Illinois at Urbana-Champaign, Urbana, IL 61801, USA.
Water Res. 2015 Sep 1;80:267-80. doi: 10.1016/j.watres.2015.05.007. Epub 2015 May 15.
Salt used to make brines for regeneration of ion exchange (IX) resins is the dominant economic and environmental liability of IX treatment systems for nitrate-contaminated drinking water sources. To reduce salt usage, the applicability and environmental benefits of using a catalytic reduction technology to treat nitrate in spent IX brines and enable their reuse for IX resin regeneration were evaluated. Hybrid IX/catalyst systems were designed and life cycle assessment of process consumables are used to set performance targets for the catalyst reactor. Nitrate reduction was measured in a typical spent brine (i.e., 5000 mg/L NO3(-) and 70,000 mg/L NaCl) using bimetallic Pd-In hydrogenation catalysts with variable Pd (0.2-2.5 wt%) and In (0.0125-0.25 wt%) loadings on pelletized activated carbon support (Pd-In/C). The highest activity of 50 mgNO3(-)/(min - g(Pd)) was obtained with a 0.5 wt%Pd-0.1 wt%In/C catalyst. Catalyst longevity was demonstrated by observing no decrease in catalyst activity over more than 60 days in a packed-bed reactor. Based on catalyst activity measured in batch and packed-bed reactors, environmental impacts of hybrid IX/catalyst systems were evaluated for both sequencing-batch and continuous-flow packed-bed reactor designs and environmental impacts of the sequencing-batch hybrid system were found to be 38-81% of those of conventional IX. Major environmental impact contributors other than salt consumption include Pd metal, hydrogen (electron donor), and carbon dioxide (pH buffer). Sensitivity of environmental impacts of the sequencing-batch hybrid reactor system to sulfate and bicarbonate anions indicate the hybrid system is more sustainable than conventional IX when influent water contains <80 mg/L sulfate (at any bicarbonate level up to 100 mg/L) or <20 mg/L bicarbonate (at any sulfate level up to 100 mg/L) assuming 15 brine reuse cycles. The study showed that hybrid IX/catalyst reactor systems have potential to reduce resource consumption and improve environmental impacts associated with treating nitrate-contaminated water sources.
用于再生离子交换 (IX) 树脂的盐水的盐是硝酸盐污染饮用水源的 IX 处理系统的主要经济和环境责任。为了减少盐的使用,评估了使用催化还原技术处理废 IX 盐水中的硝酸盐并使其可重复用于 IX 树脂再生的适用性和环境效益。设计了混合 IX/催化剂系统,并使用生命周期评估工艺消耗品来为催化剂反应器设定性能目标。在典型的废盐水中(即 5000mg/L 的 NO3(-) 和 70000mg/L 的 NaCl),使用负载在颗粒状活性炭载体 (Pd-In/C) 上的具有可变 Pd(0.2-2.5wt%)和 In(0.0125-0.25wt%)负载量的双金属 Pd-In 氢气化催化剂测量硝酸盐还原。使用 0.5wt%Pd-0.1wt%In/C 催化剂获得的 50mgNO3(-)/(min - g(Pd))的最高活性。在填充床反应器中观察到超过 60 天的催化剂活性没有下降,证明了催化剂的耐久性。基于在批处理和填充床反应器中测量的催化剂活性,评估了混合 IX/催化剂系统对顺序批处理和连续流填充床反应器设计的环境影响,发现顺序批处理混合系统的环境影响是传统 IX 的 38-81%。除盐消耗外,主要的环境影响贡献者包括 Pd 金属、氢气(电子供体)和二氧化碳(pH 缓冲剂)。对顺序批处理混合反应器系统的环境影响的敏感性硫酸盐和碳酸氢盐阴离子表明,当进水含有 <80mg/L 硫酸盐(在任何碳酸氢盐水平下高达 100mg/L)或 <20mg/L 碳酸氢盐(在任何硫酸盐水平下高达 100mg/L)时,混合系统比传统 IX 更具可持续性,假设 15 次盐水再利用循环。该研究表明,混合 IX/催化剂反应器系统具有减少处理硝酸盐污染水源相关的资源消耗和改善环境影响的潜力。