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Influence of particle size and pressure drop in cake filtration process on removal of suspended solids in anaerobically digested palm oil mill effluent

N. S. Zafisah, W. L. Ang, A. W. Mohammad, Nidal Hilal

International Journal of Engineering, Transactions B: Applications, Volume: 3, Issue: 8, Pages: 1347 - 1445

Swansea University Author: Nidal Hilal

DOI (Published version): 10.5829/ije.2018.31.08b.36

Abstract

Palm oil mill effluent (POME) poses a great threat to the environment. However, it contains valuable resources such as energy, water and nutrients that could be recovered for sustainable development. Currently, anaerobic digester has been employed to recover the energy potential in POME. However, th...

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Published in: International Journal of Engineering, Transactions B: Applications
Published: 2018
URI: https://cronfa.swan.ac.uk/Record/cronfa43772
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spelling 2018-10-30T16:26:55.1616836 v2 43772 2018-09-11 Influence of particle size and pressure drop in cake filtration process on removal of suspended solids in anaerobically digested palm oil mill effluent 3acba771241d878c8e35ff464aec0342 Nidal Hilal Nidal Hilal true false 2018-09-11 FGSEN Palm oil mill effluent (POME) poses a great threat to the environment. However, it contains valuable resources such as energy, water and nutrients that could be recovered for sustainable development. Currently, anaerobic digester has been employed to recover the energy potential in POME. However, the presence of suspended solids in the digestate hinders the downstream nutrients recovery process. In that light, cake filtration process appears to be an attractive option for the removal of suspended solids in the digestate. Hence, this paper studied the performance of cake filtration in removing suspended solids at different pressure condition and particle size of perlite. The effectiveness of cake filtration process was evaluated based on the quality of filtrate (turbidity and total suspended solids (TSS)) and filtration flux. In this study, perlites of different particle size distribution (FP3, FW6, FW20, and FW50) were used as both precoat and body feed. The amount of precoat and body feed were chosen as 1 g each. The filtration process was carried out at different pressure condition (2 - 5 bars). It was found that perlite with the finest particle size (FP3) achieved up to 90% of turbidity and TSS removal due to the formation of more compact cake filtration layer. On the other hand, larger perlite FW50 recorded lowest removal efficiency due to its porous cake layer, though this resulted in higher filtration flux. Generally, an increase in pressure resulted in higher flux but at the same time led to drastic initial flux decline due to the quick cover up of filtration voids. The outcomes from this study show that it is wise to consider the effect of particle size distribution and pressure drop in order to achieve high clarity of filtrate as well as high filtration flux. Journal Article International Journal of Engineering, Transactions B: Applications 3 8 1347 1445 1 8 2018 2018-08-01 10.5829/ije.2018.31.08b.36 COLLEGE NANME Science and Engineering - Faculty COLLEGE CODE FGSEN Swansea University 2018-10-30T16:26:55.1616836 2018-09-11T20:27:38.3343749 Faculty of Science and Engineering School of Engineering and Applied Sciences - Uncategorised N. S. Zafisah 1 W. L. Ang 2 A. W. Mohammad 3 Nidal Hilal 4 0043772-12092018150028.pdf zafisah2018(2).pdf 2018-09-12T15:00:28.2830000 Output 1369723 application/pdf Version of Record true 2018-09-12T00:00:00.0000000 true eng
title Influence of particle size and pressure drop in cake filtration process on removal of suspended solids in anaerobically digested palm oil mill effluent
spellingShingle Influence of particle size and pressure drop in cake filtration process on removal of suspended solids in anaerobically digested palm oil mill effluent
Nidal Hilal
title_short Influence of particle size and pressure drop in cake filtration process on removal of suspended solids in anaerobically digested palm oil mill effluent
title_full Influence of particle size and pressure drop in cake filtration process on removal of suspended solids in anaerobically digested palm oil mill effluent
title_fullStr Influence of particle size and pressure drop in cake filtration process on removal of suspended solids in anaerobically digested palm oil mill effluent
title_full_unstemmed Influence of particle size and pressure drop in cake filtration process on removal of suspended solids in anaerobically digested palm oil mill effluent
title_sort Influence of particle size and pressure drop in cake filtration process on removal of suspended solids in anaerobically digested palm oil mill effluent
author_id_str_mv 3acba771241d878c8e35ff464aec0342
author_id_fullname_str_mv 3acba771241d878c8e35ff464aec0342_***_Nidal Hilal
author Nidal Hilal
author2 N. S. Zafisah
W. L. Ang
A. W. Mohammad
Nidal Hilal
format Journal article
container_title International Journal of Engineering, Transactions B: Applications
container_volume 3
container_issue 8
container_start_page 1347
publishDate 2018
institution Swansea University
doi_str_mv 10.5829/ije.2018.31.08b.36
college_str Faculty of Science and Engineering
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hierarchy_top_id facultyofscienceandengineering
hierarchy_top_title Faculty of Science and Engineering
hierarchy_parent_id facultyofscienceandengineering
hierarchy_parent_title Faculty of Science and Engineering
department_str School of Engineering and Applied Sciences - Uncategorised{{{_:::_}}}Faculty of Science and Engineering{{{_:::_}}}School of Engineering and Applied Sciences - Uncategorised
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description Palm oil mill effluent (POME) poses a great threat to the environment. However, it contains valuable resources such as energy, water and nutrients that could be recovered for sustainable development. Currently, anaerobic digester has been employed to recover the energy potential in POME. However, the presence of suspended solids in the digestate hinders the downstream nutrients recovery process. In that light, cake filtration process appears to be an attractive option for the removal of suspended solids in the digestate. Hence, this paper studied the performance of cake filtration in removing suspended solids at different pressure condition and particle size of perlite. The effectiveness of cake filtration process was evaluated based on the quality of filtrate (turbidity and total suspended solids (TSS)) and filtration flux. In this study, perlites of different particle size distribution (FP3, FW6, FW20, and FW50) were used as both precoat and body feed. The amount of precoat and body feed were chosen as 1 g each. The filtration process was carried out at different pressure condition (2 - 5 bars). It was found that perlite with the finest particle size (FP3) achieved up to 90% of turbidity and TSS removal due to the formation of more compact cake filtration layer. On the other hand, larger perlite FW50 recorded lowest removal efficiency due to its porous cake layer, though this resulted in higher filtration flux. Generally, an increase in pressure resulted in higher flux but at the same time led to drastic initial flux decline due to the quick cover up of filtration voids. The outcomes from this study show that it is wise to consider the effect of particle size distribution and pressure drop in order to achieve high clarity of filtrate as well as high filtration flux.
published_date 2018-08-01T03:55:07Z
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