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		<PublisherName>Baywood Publishing Company</PublisherName>
	</PublisherInfo>
	<Journal>
		<JournalInfo JournalType="Journals">
			<JournalPrintISSN>0047-2433</JournalPrintISSN>
			<JournalElectronicISSN>1541-3802</JournalElectronicISSN>
			<JournalTitle>Journal of Environmental Systems</JournalTitle>
			<JournalCode>BWES</JournalCode>
			<JournalID>300323</JournalID>
			<JournalURL>http://baywood.metapress.com/link.asp?target=journal&amp;id=300323</JournalURL>
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		<Volume>
			<VolumeInfo>
				<VolumeNumber>24</VolumeNumber>
			</VolumeInfo>
			<Issue>
				<IssueInfo IssueType="Regular">
					<IssueNumberBegin>3</IssueNumberBegin>
					<IssueNumberEnd>3</IssueNumberEnd>
					<IssueSupplement>0</IssueSupplement>
					<IssuePartStart>0</IssuePartStart>
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					<IssueSequence>000024000319950101</IssueSequence>
					<IssuePublicationDate>
						<CoverDate Year="1995" Month="1" Day="1"/>
						<CoverDisplay>Number 3 / 1995-96</CoverDisplay>
					</IssuePublicationDate>
					<IssueID>M246JUM0W9NF</IssueID>
					<IssueURL>http://baywood.metapress.com/link.asp?target=issue&amp;id=M246JUM0W9NF</IssueURL>
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				<Article ArticleType="Original">
					<ArticleInfo Free="No" ESM="No">
						<ArticleDOI>10.2190/RK6Y-L3GB-847W-U1JW</ArticleDOI>
						<ArticlePII>RK6YL3GB847WU1JW</ArticlePII>
						<ArticleSequenceNumber>2</ArticleSequenceNumber>
						<ArticleTitle Language="En">Modeling of Sewage Circulating Reactor: An Approach to Recirculating Wastewater in Sewers</ArticleTitle>
						<ArticleFirstPage>241</ArticleFirstPage>
						<ArticleLastPage>262</ArticleLastPage>
						<ArticleHistory>
							<RegistrationDate>20020509</RegistrationDate>
							<ReceivedDate>20020509</ReceivedDate>
							<Accepted>20020509</Accepted>
							<OnlineDate>20020509</OnlineDate>
						</ArticleHistory>
						<FullTextFileName>RK6YL3GB847WU1JW.pdf</FullTextFileName>
						<FullTextURL>http://baywood.metapress.com/link.asp?target=contribution&amp;id=RK6YL3GB847WU1JW</FullTextURL>
						<Composite>3</Composite>
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					<ArticleHeader>
						<AuthorGroup>
							<Author AffiliationID="A1">
								<GivenName>Uttam</GivenName>
								<Initials>K.</Initials>
								<FamilyName>Manandhar</FamilyName>
								<Degrees/>
								<Roles/>
							</Author>
							<Author AffiliationID="A1">
								<GivenName>Hans</GivenName>
								<Initials/>
								<FamilyName>Schroder</FamilyName>
								<Degrees/>
								<Roles/>
							</Author>
							<Affiliation AFFID="A1">
								<OrgDivision/>
								<OrgName>SERD, Asian Institute of Technology, Thailand</OrgName>
								<OrgAddress/>
							</Affiliation>
						</AuthorGroup>
						<Abstract Language="En">One way to exploit the self-purifying capacity of flowing wastewater is to recirculate it so that a portion of the conveyance conduit works as a circulating biological reactor (referred to as a Sewage Circulating Reactor, SCR). This study deals with the formulation of a mathematical model for this system based on suspended-growth and biofilm kinetics. The model simulated the performance of the system satisfactorily and showed that all three biological reactions, carbon oxidation, nitrification, and denitrification, occurred simultaneously in the system. The model simulation also indicated that both suspended and film biomasses were significant at low loadings in terms of organic carbon removal. At higher loadings, suspended biomass was more significant than biofilm biomass for COD removal. The maximum substrate utilization rates (K&lt;sub&gt;m&lt;/sub&gt; values) for carbon oxidation, nitrification, and denitrification were obtained by fitting simulated profiles with the experimental ones. The k&lt;sub&gt;m&lt;/sub&gt; values for carbon oxidation and nitrification were higher for experimental runs with higher DO levels or lower loadings. However, the K&lt;sub&gt;m&lt;/sub&gt; value for denitrification was higher for the case of higher loadings.</Abstract>
						<biblist>
							<bib-other>
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								<bibtext seqNum="2">R. L. Stoyer, &lt;i&gt;The Pressure Pipe Wastewater Treatment System&lt;/i&gt;, presented to the 2nd Annual Sanitary Engineering Research Laboratory Workshop on Wastewater Reclamation and Reuse, Tahoe City, California, 1970.</bibtext>
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								<bibtext seqNum="3">C. M. Koch and J. Zandi, Use of Pipelines as Aerobic Biological Reactors, &lt;i&gt;Journal of Water Pollution Control Federation, 45&lt;/i&gt;, pp. 2537-2548, 1973.</bibtext>
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							<bib-other>
								<bibtext seqNum="4">U. K. Manandhar and H. Schroder, Sewage Circulating Reactor—An Approach to Recirculating Wastewater in Sewers, &lt;i&gt;Environment Technology Letters, 16&lt;/i&gt;, pp. 201-212, 1995.</bibtext>
							</bib-other>
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								<bibtext seqNum="5">G. H. Chen, H. Ozaki, and Y. Terashima, Modelling of the Simultaneous Removal of Organic Substances and Nitrogen in a Biofilm, &lt;i&gt;Water Science and Technology, 21&lt;/i&gt;, pp. 791-804, 1989.</bibtext>
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								<bibtext seqNum="7">P. Harremoes, Biofilm Kinetics, in &lt;i&gt;Water Pollution Microbiology&lt;/i&gt;, Vol. 2, R. Mitchell (ed.), Wiley, New York, 1978.</bibtext>
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								<bibtext seqNum="8">U. K. Manandhar, Sewage Circulating Reactor: An Approach to Recirculating Wastewater in Sewers, &lt;i&gt;Doctoral Dissertation EV-93-2&lt;/i&gt;, AIT, Bangkok, Thailand, 1993.</bibtext>
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							<bib-other>
								<bibtext seqNum="9">P. B. Saez and B. E. Rittmann, Improved Pseudoanalytical Solution for Steady-State Biofilm Kinetics, &lt;i&gt;Biotechnology and Bioengineering, 32&lt;/i&gt;, pp. 379-385, 1988.</bibtext>
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								<bibtext seqNum="10">K. J. Williamson and P. L. McCarty, Verification Studies of the Biofilm Model for Bacterial Substrate Utilization, &lt;i&gt;Journal of Water Pollution Control Federation, 48&lt;/i&gt;:2, pp. 281-296, 1976.</bibtext>
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							<bib-other>
								<bibtext seqNum="11">K. M. Brown, Computer Oriented Algorithm for Systems of Simultaneous Nonlinear Algebraic Equations, in &lt;i&gt;Numerical Solution of Systems of Nonlinear Algebraic Equations&lt;/i&gt;, G. D. Byrne and C. A. Hall (eds.), Academic Press, Orlando, Florida, 1973.</bibtext>
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							<bib-other>
								<bibtext seqNum="12">P. L. McCarty, Stoichiometry of Biological Reactions, &lt;i&gt;Progress in Water Technology, 7&lt;/i&gt;:1, pp. 157-172, 1975.</bibtext>
							</bib-other>
							<bib-other>
								<bibtext seqNum="13">E. Gonenc and P. Harremoes, Nitrification in Rotating Disc Systems: I Criteria for Transition from Oxygen to Ammonia Rate Limitation, &lt;i&gt;Water Research, 19&lt;/i&gt;:9, pp. 1119-1127, 1985.</bibtext>
							</bib-other>
							<bib-other>
								<bibtext seqNum="14">Metcalf and Eddy, Inc., &lt;i&gt;Wastewater Engineering: Treatment, Disposal, Reuse&lt;/i&gt;, McGraw Hill Book Co., New York, 1991.</bibtext>
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							<bib-other>
								<bibtext seqNum="15">E. Arvin and P. Harremoes, Concepts and Models for Biofilm Reactor Performance, &lt;i&gt;Water Science and Technology, 22&lt;/i&gt;:1/2, pp. 171-192, 1990.</bibtext>
							</bib-other>
							<bib-other>
								<bibtext seqNum="16">S. Jayamohan, S. Ohjaki, and K. Hanaki, Effect of DO on Kinetics of Nitrification, &lt;i&gt;Water Supply, 6&lt;/i&gt;, Brussels, pp. 141-150, 1988.</bibtext>
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							<bib-other>
								<bibtext seqNum="17">J. E. Alleman, Elevated Nitrite Occurrence in Biological Wastewater Treatment Systems, &lt;i&gt;Water Science and Technology, 17&lt;/i&gt;, pp. 409-419, 1984.</bibtext>
							</bib-other>
						</biblist>
					</ArticleHeader>
				</Article>
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