Skip to main content

Lund University Publications

LUND UNIVERSITY LIBRARIES

Respirometric analysis of activated sludge models from palm oil mill effluent

Damayanti, A. ; Ujang, Z. ; Salim, M. R. ; Olsson, Gustaf LU and Sulaiman, A. Z. (2010) In Bioresource Technology 101(1). p.144-149
Abstract
Activated sludge models (ASMs) have been widely used as a basis for further model development in wastewater treatment processes. Values for parameters to be used are vital for the accuracy of the modeling approach. A continuous stirred tank reactor (CSTR), as open respirometer with continuous flow for 20 h is used in ASMs. The dissolved oxygen (DO) profile for 11 days was monitored. It was found the mass transfer coefficient K-La is 0.3 h(-1) during lag and start feed phase and 0.01 h(-1) during stop feed phase, while the heterotrophic yield coefficient Y-H is 0.44. Some of the chemical oxygen demand (COD) fractionations of palm oil mill effluent (POME) using respirometric test in ASM models are S-s 50 mg/L, S-1 16,600 mg/L, X-S 25,550... (More)
Activated sludge models (ASMs) have been widely used as a basis for further model development in wastewater treatment processes. Values for parameters to be used are vital for the accuracy of the modeling approach. A continuous stirred tank reactor (CSTR), as open respirometer with continuous flow for 20 h is used in ASMs. The dissolved oxygen (DO) profile for 11 days was monitored. It was found the mass transfer coefficient K-La is 0.3 h(-1) during lag and start feed phase and 0.01 h(-1) during stop feed phase, while the heterotrophic yield coefficient Y-H is 0.44. Some of the chemical oxygen demand (COD) fractionations of palm oil mill effluent (POME) using respirometric test in ASM models are S-s 50 mg/L, S-1 16,600 mg/L, X-S 25,550 mg/L, and X-1 2,800 mg/L The comparison of experimental and ASM I from OUR concentration is found to fit well. (C) 2009 Elsevier Ltd. All rights reserved. (Less)
Please use this url to cite or link to this publication:
author
; ; ; and
organization
publishing date
type
Contribution to journal
publication status
published
subject
keywords
Respirometry test, Palm oil mill effluent, Activated sludge models, COD fractionations
in
Bioresource Technology
volume
101
issue
1
pages
144 - 149
publisher
Elsevier
external identifiers
  • wos:000271165500022
  • scopus:70349183217
  • pmid:19734044
ISSN
1873-2976
DOI
10.1016/j.biortech.2009.08.034
language
English
LU publication?
yes
id
1d6e0ff7-b787-4af8-b11e-c2c3ae6bcee2 (old id 1535776)
date added to LUP
2016-04-01 14:35:19
date last changed
2022-01-28 01:24:57
@article{1d6e0ff7-b787-4af8-b11e-c2c3ae6bcee2,
  abstract     = {{Activated sludge models (ASMs) have been widely used as a basis for further model development in wastewater treatment processes. Values for parameters to be used are vital for the accuracy of the modeling approach. A continuous stirred tank reactor (CSTR), as open respirometer with continuous flow for 20 h is used in ASMs. The dissolved oxygen (DO) profile for 11 days was monitored. It was found the mass transfer coefficient K-La is 0.3 h(-1) during lag and start feed phase and 0.01 h(-1) during stop feed phase, while the heterotrophic yield coefficient Y-H is 0.44. Some of the chemical oxygen demand (COD) fractionations of palm oil mill effluent (POME) using respirometric test in ASM models are S-s 50 mg/L, S-1 16,600 mg/L, X-S 25,550 mg/L, and X-1 2,800 mg/L The comparison of experimental and ASM I from OUR concentration is found to fit well. (C) 2009 Elsevier Ltd. All rights reserved.}},
  author       = {{Damayanti, A. and Ujang, Z. and Salim, M. R. and Olsson, Gustaf and Sulaiman, A. Z.}},
  issn         = {{1873-2976}},
  keywords     = {{Respirometry test; Palm oil mill effluent; Activated sludge models; COD fractionations}},
  language     = {{eng}},
  number       = {{1}},
  pages        = {{144--149}},
  publisher    = {{Elsevier}},
  series       = {{Bioresource Technology}},
  title        = {{Respirometric analysis of activated sludge models from palm oil mill effluent}},
  url          = {{http://dx.doi.org/10.1016/j.biortech.2009.08.034}},
  doi          = {{10.1016/j.biortech.2009.08.034}},
  volume       = {{101}},
  year         = {{2010}},
}