Foulant analysis in cross-flow filtration using resistancein-series model

Membrane technologies grow rapidly in the world and were applied in many industrial processes as an efficient separation technique and for the purpose of wastewater treatment. Membrane separation process was used to replace the conventional method to reduce time of operation, reduce space requiremen...

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Main Author: Nurul Hidayah, Muhamad
Format: Undergraduates Project Papers
Language:English
Published: 2010
Subjects:
Online Access:http://umpir.ump.edu.my/id/eprint/3243/
http://umpir.ump.edu.my/id/eprint/3243/
http://umpir.ump.edu.my/id/eprint/3243/1/CD5816_NURUL_HIDAYAH_MUHAMMAD.pdf
id ump-3243
recordtype eprints
spelling ump-32432015-03-03T08:00:08Z http://umpir.ump.edu.my/id/eprint/3243/ Foulant analysis in cross-flow filtration using resistancein-series model Nurul Hidayah, Muhamad TP Chemical technology Membrane technologies grow rapidly in the world and were applied in many industrial processes as an efficient separation technique and for the purpose of wastewater treatment. Membrane separation process was used to replace the conventional method to reduce time of operation, reduce space requirement for downstream process and increase the productivity. There are several types of membrane separation used in the industries which are ultrafiltration, microfiltration, nanofiltration and reverse osmosis. These membrane separations used different types of membrane such as flat sheet, hollow fiber and other. Even though membrane separation has many advantages, it also has a problem which is membrane fouling that resulting in reduces permeate flux and increase the production cost. This study is undertaken to identify and determine the resistances that lead membrane fouling by using Resistance-In-Series Model and Darcy’s Law. A cross-flow filtration with polysulfone hollow fiber membrane of molecular pore size 0.2μm was used to separate the buffer solution containing Escherichia coli. From the data obtained, the weak adsorption resistance was explored as the main factor resulting membrane fouling in this study. For the membrane recovery, the alkaline cleaning can recover the fouled membrane about 99.8% and it could help increasing the permeate flux for separation process. E. coli K-12 strain was identified which can give high permeate flux compared to E. coli B strain. Thus, E. coli K-12 can be retained by membrane in the separation of succinic acid from fermentation broth. 2010-04 Undergraduates Project Papers NonPeerReviewed application/pdf en http://umpir.ump.edu.my/id/eprint/3243/1/CD5816_NURUL_HIDAYAH_MUHAMMAD.pdf Nurul Hidayah, Muhamad (2010) Foulant analysis in cross-flow filtration using resistancein-series model. Faculty of Chemical & Natural Resources Engineering , Universiti Malaysia Pahang . http://iportal.ump.edu.my/lib/item?id=chamo:58561&theme=UMP2
repository_type Digital Repository
institution_category Local University
institution Universiti Malaysia Pahang
building UMP Institutional Repository
collection Online Access
language English
topic TP Chemical technology
spellingShingle TP Chemical technology
Nurul Hidayah, Muhamad
Foulant analysis in cross-flow filtration using resistancein-series model
description Membrane technologies grow rapidly in the world and were applied in many industrial processes as an efficient separation technique and for the purpose of wastewater treatment. Membrane separation process was used to replace the conventional method to reduce time of operation, reduce space requirement for downstream process and increase the productivity. There are several types of membrane separation used in the industries which are ultrafiltration, microfiltration, nanofiltration and reverse osmosis. These membrane separations used different types of membrane such as flat sheet, hollow fiber and other. Even though membrane separation has many advantages, it also has a problem which is membrane fouling that resulting in reduces permeate flux and increase the production cost. This study is undertaken to identify and determine the resistances that lead membrane fouling by using Resistance-In-Series Model and Darcy’s Law. A cross-flow filtration with polysulfone hollow fiber membrane of molecular pore size 0.2μm was used to separate the buffer solution containing Escherichia coli. From the data obtained, the weak adsorption resistance was explored as the main factor resulting membrane fouling in this study. For the membrane recovery, the alkaline cleaning can recover the fouled membrane about 99.8% and it could help increasing the permeate flux for separation process. E. coli K-12 strain was identified which can give high permeate flux compared to E. coli B strain. Thus, E. coli K-12 can be retained by membrane in the separation of succinic acid from fermentation broth.
format Undergraduates Project Papers
author Nurul Hidayah, Muhamad
author_facet Nurul Hidayah, Muhamad
author_sort Nurul Hidayah, Muhamad
title Foulant analysis in cross-flow filtration using resistancein-series model
title_short Foulant analysis in cross-flow filtration using resistancein-series model
title_full Foulant analysis in cross-flow filtration using resistancein-series model
title_fullStr Foulant analysis in cross-flow filtration using resistancein-series model
title_full_unstemmed Foulant analysis in cross-flow filtration using resistancein-series model
title_sort foulant analysis in cross-flow filtration using resistancein-series model
publishDate 2010
url http://umpir.ump.edu.my/id/eprint/3243/
http://umpir.ump.edu.my/id/eprint/3243/
http://umpir.ump.edu.my/id/eprint/3243/1/CD5816_NURUL_HIDAYAH_MUHAMMAD.pdf
first_indexed 2023-09-18T21:57:22Z
last_indexed 2023-09-18T21:57:22Z
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