Activated carbon minimization in two-stage batch adsorption without intermediate adsorbent separation to treat real industrial wastewater containing phenolic compounds

IF 3.9 3区 工程技术 Q2 ENGINEERING, CHEMICAL
Rogério Felito da Silva, Luís A.M. Ruotolo
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Abstract

The need to treat industrial effluents containing toxic substances has stimulated the search for alternative strategies that can reduce process costs. Among these pollutants, phenolic compounds present a high risk to human health and the environment. The present work explores strategies to minimize costs and the consumption of commercial activated carbons in batch adsorption processes, proposing the use of a new two-stage adsorption approach without intermediate filtration to separate the exhausted adsorbent. Investigation of the thermodynamics and kinetics of these processes enabled the understanding of operational fundamentals that allowed the identification of application niches and the proposal of optimization procedures. Firstly, phenol was used as a model molecule to develop adsorption strategies that minimized the adsorbent dosage and cost, which were then validated using real industrial effluents containing phenolic compounds. Evaluation was made of the effects of operational parameters such as contact time and pH, using different adsorbents. The optimal contact time varied according to the adsorbent uptake capacity, which varied from 23.53 mg g−1 to 146.4 mg g−1 for the different carbons evaluated, while the highest efficiencies were achieved at pH between 3 and 4. The viability of applying the two-stage process without intermediate filtration depended on the capacity of the adsorbent added in the first stage to retain the adsorbed solute, being appropriated for application in industrial processes where the effluent composition does not vary significantly, while the two-stage approach with intermediate filtration could potentially reduce the process cost by 33 %, compared to the conventional one-stage method. The findings are expected to benefit companies operating in the sector, offering ways to reduce adsorbent consumption and minimize environmental impacts.
活性炭在两级间歇吸附中的最小化,无需中间吸附剂分离处理含酚类化合物的实际工业废水
处理含有有毒物质的工业废水的需要促使人们寻找能够降低处理成本的替代战略。在这些污染物中,酚类化合物对人类健康和环境具有很高的风险。本研究探讨了在间歇吸附过程中降低成本和商用活性炭消耗的策略,提出了一种新的两阶段吸附方法,不需要中间过滤来分离耗尽的吸附剂。对这些过程的热力学和动力学的研究使我们能够理解操作基础,从而确定应用领域并提出优化程序。首先,以苯酚为模型分子,开发吸附策略,以最大限度地减少吸附剂的用量和成本,然后使用含有酚类化合物的实际工业废水进行验证。考察了不同吸附剂对接触时间、pH等操作参数的影响。最佳接触时间随吸附剂吸附量的变化而变化,不同碳的吸附量为23.53 mg g−1 ~ 146.4 mg g−1,pH值为3 ~ 4时吸附效率最高。采用不采用中间过滤的两级工艺的可行性取决于在第一级添加的吸附剂保留吸附溶质的能力,适用于污水成分变化不大的工业过程,而采用中间过滤的两级方法与传统的一级方法相比,可能会降低33 %的工艺成本。研究结果有望使该行业的公司受益,为减少吸附剂的消耗和最大限度地减少对环境的影响提供了方法。
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来源期刊
Chemical Engineering Research & Design
Chemical Engineering Research & Design 工程技术-工程:化工
CiteScore
6.10
自引率
7.70%
发文量
623
审稿时长
42 days
期刊介绍: ChERD aims to be the principal international journal for publication of high quality, original papers in chemical engineering. Papers showing how research results can be used in chemical engineering design, and accounts of experimental or theoretical research work bringing new perspectives to established principles, highlighting unsolved problems or indicating directions for future research, are particularly welcome. Contributions that deal with new developments in plant or processes and that can be given quantitative expression are encouraged. The journal is especially interested in papers that extend the boundaries of traditional chemical engineering.
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