Adsorption - Membrane process for treatment of stabilized municipal landfill leachate

被引:22
|
作者
Zielinska, Magdalena [1 ]
Kulikowska, Dorota [1 ]
Stanczak, Marcin [1 ]
机构
[1] Univ Warmia & Mazury, Fac Geoengn, Dept Environm Biotechnol, 45G Sloneczna St, PL-10907 Olsztyn, Poland
关键词
Powdered activated carbon; Microfiltration (MF); Ultrafiltration (UF); Fine-ultrafiltration (fine-UF); Ceramic membranes; POWDERED ACTIVATED CARBON; SEQUENCING BATCH REACTOR; SOLID-WASTE LANDFILL; HUMIC ACIDS; ORGANIC-COMPOUNDS; NITROGEN REMOVAL; WATER-TREATMENT; HYBRID SYSTEM; MICROFILTRATION; NANOFILTRATION;
D O I
10.1016/j.wasman.2020.07.011
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
The aim of this study was to investigate the efficiency of removal of difficult-to-biodegrade organic compounds from real stabilized landfill leachate with a membrane process alone and in combination with powdered-activated-carbon (PAC) adsorption. For filtration, ceramic membranes were used. The characteristics of the raw leachate were 788 mg COD/L and color of 0.4458 cm(-1). With all combinations of PAC-adsorption and a membrane process (MF, UF, fine-UF) and with fine-UF alone, leachate treatment was highly efficient. For each membrane, treatment was more efficient when the membrane process was combined with PAC addition. This means that adsorption (PAC dose 3 g/L, adsorption time 30 min) made the largest contribution to leachate treatment (COD and color removal efficiency of 73.1% and 94.4%, respectively). In all cases, organic particles bigger than 100 kDa were removed most efficiently, whereas particles smaller than 3 kDa were removed least efficiently. The efficiency of leachate treatment with PAC + MF, PAC + UF and PAC + fine-UF did not differ significantly (>87% COD and > 97% color). With regard to membrane flux, however, these combinations can be ranked in the following order: PAC + MF > PAC + UF > PAC + fine-UF. Therefore, PAC + MF (0.3 MPa) was selected as the most effective solution (COD and color removal efficiencies of 87.8% and 97.2%, respectively; permeate flux of 167.6 L/(m(2).h)), as it combined efficient pollutant removal with low membrane pressure. (C) 2020 Elsevier Ltd. All rights reserved.
引用
收藏
页码:174 / 182
页数:9
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