Intensified Niagara leaf filtration via in-situ ultrasonic wave fields

Niagara Leaf Filter unit is commonly used for the separation of bleaching agent from the `Refined Bleached Deodorized' (RBD) oil in the edible/vegetable oil industry. In general, the time required to separate 500 kg bleaching agent from the treated oil is approximately 2 ½ hours after which th...

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Main Authors: Mohd Yunus, Rosli, Junin, Radzuan, Sulaiman, Ahmad Ziad, Abdul Aziz, Ramlan, Ngah, Mokhtar, Nasir, Abu Samah, Sethpa, Mohd Sabri
Format: Article
Language:English
Published: Faculty of Chemical and Natural Resources Engineering, UTM 2001
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Online Access:http://eprints.utm.my/id/eprint/5076/1/RosliMohdYunus2001_IntensifiedNiagaraLeafFiltration.pdf
http://eprints.utm.my/id/eprint/5076/
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spelling my.utm.50762010-06-01T03:23:17Z http://eprints.utm.my/id/eprint/5076/ Intensified Niagara leaf filtration via in-situ ultrasonic wave fields Mohd Yunus, Rosli Junin, Radzuan Sulaiman, Ahmad Ziad Abdul Aziz, Ramlan Ngah, Mokhtar Nasir, Abu Samah Sethpa, Mohd Sabri T Technology (General) Niagara Leaf Filter unit is commonly used for the separation of bleaching agent from the `Refined Bleached Deodorized' (RBD) oil in the edible/vegetable oil industry. In general, the time required to separate 500 kg bleaching agent from the treated oil is approximately 2 ½ hours after which the system is totally filled with solid particles and the system needs to be regenerated. A typical regeneration process of the system takes approximately 1½ hours. The sequence of filtration and regeneration process is repeated for approximately two to three weeks, depending on the condition of the filter medium, before a thorough cleaning method is conducted which last for a period of five to seven days. In view of the long downtime of the filtering operation system, this study is conducted to investigate the possibility of intensifying the filtration operation with the assistance of ultrasound wave fields. In this paper, the effect of ultrasound on the rate of filtration of activated clay in oil suspension is presented. The degree of filtration rate enhancement as a function of solids concentration in the feed is also discussed. In general, the ultrasound field improves the filtration rate by minimizing the thickness of the filter cake, and hence reducing the resistance of fluid flowing through the filter medium. The solids concentration has a negative impact on the degree of filtration improvement as a result of ultrasound wave fields. Faculty of Chemical and Natural Resources Engineering, UTM 2001 Article PeerReviewed application/pdf en http://eprints.utm.my/id/eprint/5076/1/RosliMohdYunus2001_IntensifiedNiagaraLeafFiltration.pdf Mohd Yunus, Rosli and Junin, Radzuan and Sulaiman, Ahmad Ziad and Abdul Aziz, Ramlan and Ngah, Mokhtar and Nasir, Abu Samah and Sethpa, Mohd Sabri (2001) Intensified Niagara leaf filtration via in-situ ultrasonic wave fields. Proceedings of The 15th Symposium of Malaysian Chemical Engineers SOMChE 2001 . pp. 531-535.
institution Universiti Teknologi Malaysia
building UTM Library
collection Institutional Repository
continent Asia
country Malaysia
content_provider Universiti Teknologi Malaysia
content_source UTM Institutional Repository
url_provider http://eprints.utm.my/
language English
topic T Technology (General)
spellingShingle T Technology (General)
Mohd Yunus, Rosli
Junin, Radzuan
Sulaiman, Ahmad Ziad
Abdul Aziz, Ramlan
Ngah, Mokhtar
Nasir, Abu Samah
Sethpa, Mohd Sabri
Intensified Niagara leaf filtration via in-situ ultrasonic wave fields
description Niagara Leaf Filter unit is commonly used for the separation of bleaching agent from the `Refined Bleached Deodorized' (RBD) oil in the edible/vegetable oil industry. In general, the time required to separate 500 kg bleaching agent from the treated oil is approximately 2 ½ hours after which the system is totally filled with solid particles and the system needs to be regenerated. A typical regeneration process of the system takes approximately 1½ hours. The sequence of filtration and regeneration process is repeated for approximately two to three weeks, depending on the condition of the filter medium, before a thorough cleaning method is conducted which last for a period of five to seven days. In view of the long downtime of the filtering operation system, this study is conducted to investigate the possibility of intensifying the filtration operation with the assistance of ultrasound wave fields. In this paper, the effect of ultrasound on the rate of filtration of activated clay in oil suspension is presented. The degree of filtration rate enhancement as a function of solids concentration in the feed is also discussed. In general, the ultrasound field improves the filtration rate by minimizing the thickness of the filter cake, and hence reducing the resistance of fluid flowing through the filter medium. The solids concentration has a negative impact on the degree of filtration improvement as a result of ultrasound wave fields.
format Article
author Mohd Yunus, Rosli
Junin, Radzuan
Sulaiman, Ahmad Ziad
Abdul Aziz, Ramlan
Ngah, Mokhtar
Nasir, Abu Samah
Sethpa, Mohd Sabri
author_facet Mohd Yunus, Rosli
Junin, Radzuan
Sulaiman, Ahmad Ziad
Abdul Aziz, Ramlan
Ngah, Mokhtar
Nasir, Abu Samah
Sethpa, Mohd Sabri
author_sort Mohd Yunus, Rosli
title Intensified Niagara leaf filtration via in-situ ultrasonic wave fields
title_short Intensified Niagara leaf filtration via in-situ ultrasonic wave fields
title_full Intensified Niagara leaf filtration via in-situ ultrasonic wave fields
title_fullStr Intensified Niagara leaf filtration via in-situ ultrasonic wave fields
title_full_unstemmed Intensified Niagara leaf filtration via in-situ ultrasonic wave fields
title_sort intensified niagara leaf filtration via in-situ ultrasonic wave fields
publisher Faculty of Chemical and Natural Resources Engineering, UTM
publishDate 2001
url http://eprints.utm.my/id/eprint/5076/1/RosliMohdYunus2001_IntensifiedNiagaraLeafFiltration.pdf
http://eprints.utm.my/id/eprint/5076/
_version_ 1643644230162186240
score 13.188404