Cation exchanger mixed matrix membrane (MMM) for lead (II) removal from wastewater

Many toxic heavy metals have been discharged into the environment as industrial wastes everyday.In all over the world,industry is forced by the regulation body to diminish down the heavy metal content to the acceptable level in their wastewaters effluents.In the current research,cation exchanger mix...

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Main Author: Nurul Farhana, Mohamed Basri
Format: Undergraduates Project Papers
Language:English
Published: 2012
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Online Access:http://umpir.ump.edu.my/id/eprint/4343/1/03.Cation%20exchanger%20mixed%20matrix%20membrane%20%28MMM%29%20for%20lead%20%28II%29%20removal%20from%20wastewater.pdf
http://umpir.ump.edu.my/id/eprint/4343/
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Institution: Universiti Malaysia Pahang
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spelling my.ump.umpir.43432023-07-05T02:02:00Z http://umpir.ump.edu.my/id/eprint/4343/ Cation exchanger mixed matrix membrane (MMM) for lead (II) removal from wastewater Nurul Farhana, Mohamed Basri TP Chemical technology Many toxic heavy metals have been discharged into the environment as industrial wastes everyday.In all over the world,industry is forced by the regulation body to diminish down the heavy metal content to the acceptable level in their wastewaters effluents.In the current research,cation exchanger mixed matrix membrane (MMM) was developed for the lead (Pb) removal from wastewater.A list of commercial cation resin was screened for highest Pb removal.These resins include Dowex M-31,Dowex MAC-3,Amberlite IR-120, Lewatit SP 112,Amberlite IRC-86, Lewatit TP-214,Amberlite IRN-150 and Dowex Marathon MSC.Dowex M-31 cation resin was incorporated into ethylene vinyl alcohol based polymer at different resin loading range from 10 – 30 weight % to prepare cation MMM.In a batch experiment,several parameters were optimized including Pb (II) concentration between 100 to 2000 mg/L,pH between 1 to 8,contact time between 3 to 12 hours and the amount of absorbent from 0.1 to 1 g. Adsorption isotherm for the cation MMM and ground resin were follow to Langmuir isotherm.The increase in resin loading will increase the binding capacity of cation MMM up to a limitation of 50 wt% resin loading.The concept of MMM was successfully expanded to the application of heavy metal removal. 2012-03 Undergraduates Project Papers NonPeerReviewed pdf en http://umpir.ump.edu.my/id/eprint/4343/1/03.Cation%20exchanger%20mixed%20matrix%20membrane%20%28MMM%29%20for%20lead%20%28II%29%20removal%20from%20wastewater.pdf Nurul Farhana, Mohamed Basri (2012) Cation exchanger mixed matrix membrane (MMM) for lead (II) removal from wastewater. Faculty of Chemical & Natural Resource Engineering, Universiti Malaysia Pahang.
institution Universiti Malaysia Pahang
building UMP Library
collection Institutional Repository
continent Asia
country Malaysia
content_provider Universiti Malaysia Pahang
content_source UMP Institutional Repository
url_provider http://umpir.ump.edu.my/
language English
topic TP Chemical technology
spellingShingle TP Chemical technology
Nurul Farhana, Mohamed Basri
Cation exchanger mixed matrix membrane (MMM) for lead (II) removal from wastewater
description Many toxic heavy metals have been discharged into the environment as industrial wastes everyday.In all over the world,industry is forced by the regulation body to diminish down the heavy metal content to the acceptable level in their wastewaters effluents.In the current research,cation exchanger mixed matrix membrane (MMM) was developed for the lead (Pb) removal from wastewater.A list of commercial cation resin was screened for highest Pb removal.These resins include Dowex M-31,Dowex MAC-3,Amberlite IR-120, Lewatit SP 112,Amberlite IRC-86, Lewatit TP-214,Amberlite IRN-150 and Dowex Marathon MSC.Dowex M-31 cation resin was incorporated into ethylene vinyl alcohol based polymer at different resin loading range from 10 – 30 weight % to prepare cation MMM.In a batch experiment,several parameters were optimized including Pb (II) concentration between 100 to 2000 mg/L,pH between 1 to 8,contact time between 3 to 12 hours and the amount of absorbent from 0.1 to 1 g. Adsorption isotherm for the cation MMM and ground resin were follow to Langmuir isotherm.The increase in resin loading will increase the binding capacity of cation MMM up to a limitation of 50 wt% resin loading.The concept of MMM was successfully expanded to the application of heavy metal removal.
format Undergraduates Project Papers
author Nurul Farhana, Mohamed Basri
author_facet Nurul Farhana, Mohamed Basri
author_sort Nurul Farhana, Mohamed Basri
title Cation exchanger mixed matrix membrane (MMM) for lead (II) removal from wastewater
title_short Cation exchanger mixed matrix membrane (MMM) for lead (II) removal from wastewater
title_full Cation exchanger mixed matrix membrane (MMM) for lead (II) removal from wastewater
title_fullStr Cation exchanger mixed matrix membrane (MMM) for lead (II) removal from wastewater
title_full_unstemmed Cation exchanger mixed matrix membrane (MMM) for lead (II) removal from wastewater
title_sort cation exchanger mixed matrix membrane (mmm) for lead (ii) removal from wastewater
publishDate 2012
url http://umpir.ump.edu.my/id/eprint/4343/1/03.Cation%20exchanger%20mixed%20matrix%20membrane%20%28MMM%29%20for%20lead%20%28II%29%20removal%20from%20wastewater.pdf
http://umpir.ump.edu.my/id/eprint/4343/
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