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231225s2020 xx |||||o 00| ||eng c |
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|a 10.1016/j.wasman.2020.07.011
|2 doi
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|a pubmed25n1041.xml
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|a (PII)S0956-053X(20)30377-9
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|a DE-627
|b ger
|c DE-627
|e rakwb
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|a eng
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|a Zielińska, Magdalena
|e verfasserin
|4 aut
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|a Adsorption - Membrane process for treatment of stabilized municipal landfill leachate
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|c 2020
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|a Text
|b txt
|2 rdacontent
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|a ƒaComputermedien
|b c
|2 rdamedia
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|a ƒa Online-Ressource
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|2 rdacarrier
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|a Date Completed 04.08.2020
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|a Date Revised 04.08.2020
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|a published: Print-Electronic
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|a Citation Status MEDLINE
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|a Copyright © 2020 Elsevier Ltd. All rights reserved.
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|a 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/(m2∙h)), as it combined efficient pollutant removal with low membrane pressure
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|a Journal Article
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|a Ceramic membranes
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|a Fine-ultrafiltration (fine-UF)
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|a Microfiltration (MF)
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|a Powdered activated carbon
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|a Ultrafiltration (UF)
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|a Membranes, Artificial
|2 NLM
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|a Water Pollutants, Chemical
|2 NLM
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|a Charcoal
|2 NLM
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|a 16291-96-6
|2 NLM
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|a Kulikowska, Dorota
|e verfasserin
|4 aut
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|a Stańczak, Marcin
|e verfasserin
|4 aut
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|i Enthalten in
|t Waste management (New York, N.Y.)
|d 1999
|g 114(2020) vom: 01. Aug., Seite 174-182
|w (DE-627)NLM098197061
|x 1879-2456
|7 nnas
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|g volume:114
|g year:2020
|g day:01
|g month:08
|g pages:174-182
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|u http://dx.doi.org/10.1016/j.wasman.2020.07.011
|3 Volltext
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|d 114
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|b 01
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|h 174-182
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