You are not logged in.

Powdered activated carbon for fouling reduction of membrane in a pilot-scale recirculation aquaculture system

Jegatheesan, V., Senaratne, N., Steicke, C. and Kim, Seung-Hyun 2009, Powdered activated carbon for fouling reduction of membrane in a pilot-scale recirculation aquaculture system, Desalination and Water Treatment, vol. 5, pp. 1-5.

Attached Files
Name Description MIMEType Size Downloads

Title Powdered activated carbon for fouling reduction of membrane in a pilot-scale recirculation aquaculture system
Author(s) Jegatheesan, V.
Senaratne, N.
Steicke, C.
Kim, Seung-Hyun
Journal name Desalination and Water Treatment
Volume number 5
Start page 1
End page 5
Total pages 5
Publisher Balaban Publishers
Place of publication Hopkinton, Mass.
Publication date 2009-05
ISSN 1944-3994
1944-3986
Keyword(s) denitrification
transmembrane pressure (TMP)
recirculating aquaculture system (RAS)
powdered activated carbon (PAC)
membrane bioreactor (MBR)
fouling
Summary Recirculating aquaculture systems (RAS) are essential for the reduction in fresh water usage as well as the discharge of nutrients along with aquaculture effluents. A RAS consisting of an anoxic reactor, a membrane bioreactor (MBR) and a UV-disinfection unit was used to process 10,000 L/d of aquaculture effluent providing high-quality treated water for recirculation to a Barramundi fish culture. The system maintained low levels of nitrate (<20 mg/L), nitrite (<3 mg/L) and ammonia (<0.6 mg/L) in the fish tank. Permeate from the membrane that was recirculated to the fish tank contained <21 mg/L of nitrate, <2 mg/L of nitrite and 0 mg/L of ammonia. However, the rate of fouling of the membrane in the MBR was around 1.47 kPa/d, and the membrane in the MBR required cleaning due to fouling after 16 days. Cleaning of the membrane was initiated when the TMP reached around 25 to 30 kPa. In order to reduce the rate of fouling, 500 mg of powdered activated carbon (PAC) per litre of MBR volume was introduced, which decreased the rate of fouling to 0.90 kPa/d. Cleaning of membrane was needed only after 31 days of operation while maintaining the treated effluent quality. Thus the frequency of cleaning could be halved due to the introduction of PAC into the MBR.
Notes Presented at EuroMed 2008, Desalination for Clean Water and Energy Cooperation among Mediterranean Countries of Europe and the MENA Region, 9–13 November 2008, King Hussein Bin Talal Convention Center, Dead Sea, Jordan.
Language eng
Field of Research 099999 Engineering not elsewhere classified
Socio Economic Objective 970109 Expanding Knowledge in Engineering
HERDC Research category C1.1 Refereed article in a scholarly journal
Copyright notice ©2009, Balaban Publishers
Persistent URL http://hdl.handle.net/10536/DRO/DU:30039694

Document type: Journal Article
Collection: School of Engineering
Connect to link resolver
 
Unless expressly stated otherwise, the copyright for items in DRO is owned by the author, with all rights reserved.

Versions
Version Filter Type
Citation counts: TR Web of Science Citation Count  Cited 0 times in TR Web of Science
Scopus Citation Count Cited 3 times in Scopus
Google Scholar Search Google Scholar
Access Statistics: 77 Abstract Views, 0 File Downloads  -  Detailed Statistics
Created: Thu, 27 Oct 2011, 08:59:58 EST

Every reasonable effort has been made to ensure that permission has been obtained for items included in DRO. If you believe that your rights have been infringed by this repository, please contact drosupport@deakin.edu.au.