Leachate treatment via electrocoagulation-coal-based powdered activated carbon process: Efficiencies, mechanisms, kinetics, and costs.

IF 2.5 4区 环境科学与生态学 Q3 ENGINEERING, ENVIRONMENTAL
Aysenur Ogedey, Ensar Oguz
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引用次数: 0

Abstract

This study aims to improve COD, NH3-N, and turbidity removal from Bingöl's leachate using a single-reactor integrated electrocoagulation (EC)-coal-based powdered activated carbon (CBPAC) process under various experimental conditions. In the EC-CBPAC process, three stainless-steel cathodes and three aluminum electrodes were connected to the negative and positive terminals of the power supply, respectively. The initial concentrations in the leachate were 1044 mg O2/L for COD, 204 mg/L for NH3-N, and 57 NTU (or 71.25-mg (NH2)2H2SO4/L) for turbidity, respectively. After a 40-min EC-CBPAC process, with a CBPAC dosage of 5 g/L and pH of 5 for COD and turbidity, and 9.5 for NH3-N, the optimum removal efficiencies for COD, NH3-N, and turbidity were achieved at 92%, 40%, and 91%, respectively. When the EC process was applied without CBPAC under the same experimental conditions, the removal efficiencies of COD, NH3-N, and turbidity were 87%, 28%, and 54%, respectively. Before and after the EC-CBPAC process, the Brunauer-Emmett-Teller (BET) surface area, pore volume, and mean pore diameter of the CBPAC were found to be (888 m2/g, 0.498 cm3/g, and 22.28 Å) and (173 m2/g, 0.18 cm3/g, and 42.8 Å), respectively. The optimum pseudo-first-order (PFO) rate constants for COD, turbidity, and NH3-N were determined to be 3.15 × 10-2, 4.77 × 10-2, and 8.8 × 10-3 min-1, respectively. With the current density increasing from 15 to 25 mA/cm2, energy consumption, unit energy consumption, and total cost increased from 68.7 to 122.4 kWh/m3, 6.948 to 15.226 kWh/kg COD, and 0.85 to 1.838 $/kg COD, respectively. PRACTITIONER POINTS: EC-CBPAC process has greater COD, NH3-N, and turbidity removal efficiency than EC process. COD and turbidity achieved their optimum disposal efficiencies at 92% and 91%, respectively, at pH 5 The most efficient disposal efficiency for NH3-N was observed to be 40% at pH 9.5. EC-CBPAC process increased removal efficiencies for COD, NH3-N, and turbidity by 20%, 19%, and 38%, respectively, compared with EC alone. The turbidity, NH3-N, and COD disposal fitted PSO model due to high correlation values (R2 0.94-0.99).

通过电凝-煤基粉末活性炭工艺处理渗滤液:效率、机制、动力学和成本。
本研究旨在利用单反应器集成电凝(EC)-炭基粉末活性炭(CBPAC)工艺,在各种实验条件下提高宾格尔垃圾渗滤液中 COD、NH3-N 和浊度的去除率。在 EC-CBPAC 工艺中,电源的正负极分别连接了三个不锈钢阴极和三个铝电极。渗滤液中 COD 的初始浓度为 1044 mg O2/L,NH3-N 为 204 mg/L,浊度为 57 NTU(或 71.25 mg (NH2)2H2SO4/L)。经过 40 分钟的 EC-CBPAC 工艺后,CBPAC 投加量为 5 克/升,COD 和浊度的 pH 值为 5,NH3-N 为 9.5,COD、NH3-N 和浊度的最佳去除率分别为 92%、40% 和 91%。在相同的实验条件下,在不使用 CBPAC 的情况下使用 EC 工艺时,COD、NH3-N 和浊度的去除率分别为 87%、28% 和 54%。在 EC-CBPAC 工艺前后,CBPAC 的布鲁纳-埃美特-泰勒(BET)表面积、孔体积和平均孔直径分别为(888 m2/g、0.498 cm3/g 和 22.28 Å)和(173 m2/g、0.18 cm3/g 和 42.8 Å)。经测定,COD、浊度和 NH3-N 的最佳伪一阶 (PFO) 率常数分别为 3.15 × 10-2、4.77 × 10-2 和 8.8 × 10-3 min-1。随着电流密度从 15 mA/cm2 增加到 25 mA/cm2,能耗、单位能耗和总成本分别从 68.7 kWh/m3 增加到 122.4 kWh/m3、6.948 kWh/kg COD 增加到 15.226 kWh/kg、0.85 美元/kg COD 增加到 1.838 美元/kg。实践点:EC-CBPAC 工艺的 COD、NH3-N 和浊度去除效率高于 EC 工艺。在 pH 值为 5 时,COD 和浊度的最佳去除率分别为 92% 和 91%。与单独使用 EC 相比,EC-CBPAC 工艺对 COD、NH3-N 和浊度的去除率分别提高了 20%、19% 和 38%。浊度、NH3-N 和 COD 的去除率与 PSO 模型的相关性很高(R2 为 0.94-0.99)。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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来源期刊
Water Environment Research
Water Environment Research 环境科学-工程:环境
CiteScore
6.30
自引率
0.00%
发文量
138
审稿时长
11 months
期刊介绍: Published since 1928, Water Environment Research (WER) is an international multidisciplinary water resource management journal for the dissemination of fundamental and applied research in all scientific and technical areas related to water quality and resource recovery. WER''s goal is to foster communication and interdisciplinary research between water sciences and related fields such as environmental toxicology, agriculture, public and occupational health, microbiology, and ecology. In addition to original research articles, short communications, case studies, reviews, and perspectives are encouraged.
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