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<ArticleSet>
<Article>
<Journal>
				<PublisherName>Iranian Association of Chemical Engineering (IAChE)</PublisherName>
				<JournalTitle>Iranian Journal of Chemical Engineering (IJChE)</JournalTitle>
				<Issn>1735-5397</Issn>
				<Volume>7</Volume>
				<Issue>1</Issue>
				<PubDate PubStatus="epublish">
					<Year>2010</Year>
					<Month>01</Month>
					<Day>01</Day>
				</PubDate>
			</Journal>
<ArticleTitle>Looped Pipeline System for Increasing the Capacity of Natural Gas Transmission</ArticleTitle>
<VernacularTitle></VernacularTitle>
			<FirstPage>76</FirstPage>
			<LastPage>86</LastPage>
			<ELocationID EIdType="pii">10349</ELocationID>
			
			
			<Language>EN</Language>
<AuthorList>
<Author>
					<FirstName>M. A.</FirstName>
					<LastName>Fanaei</LastName>
<Affiliation>Department of Chemical Engineering, Faculty of Eng., Ferdowsi University of Mashhad, I. R.Iran</Affiliation>

</Author>
<Author>
					<FirstName>M.</FirstName>
					<LastName>Niknam</LastName>
<Affiliation></Affiliation>

</Author>
</AuthorList>
				<PublicationType>Journal Article</PublicationType>
			<History>
				<PubDate PubStatus="received">
					<Year>2015</Year>
					<Month>08</Month>
					<Day>03</Day>
				</PubDate>
			</History>
		<Abstract>At present, gas engineers use the simple Campbell’s equation to determine the proper length of parallel gas pipelines. The Campbell’s equation was proposed for horizontal pipelines with the assumption that the gas compressibility factor and temperature throughout the pipeline are constant. Therefore, the Campbell’s equation has a notable error for an inclined pipeline. In this paper, the Campbell’s equation was extended in a way that it can be used for inclined pipelines. In order to make a comparison between the extended and original equations, a pipeline with different slopes was used. The results show that in the case of using a pipeline with more than 2 degrees in slope, the resultant error is increased to 11 percent by using the original Campbell’s equation. For validation of the extended Campbell’s equation, the results of this equation are compared to the results of HYSYS software (version 3.1) in which the temperature and gas compressibility factor are not considered constant. The results indicate that the average error of the extended equation is less than 2 percent.</Abstract>
		<ObjectList>
			<Object Type="keyword">
			<Param Name="value">natural gas pipeline</Param>
			</Object>
			<Object Type="keyword">
			<Param Name="value">Looped Pipeline</Param>
			</Object>
			<Object Type="keyword">
			<Param Name="value">optimization</Param>
			</Object>
		</ObjectList>
<ArchiveCopySource DocType="pdf">https://www.ijche.com/article_10349_f8a4c7893a5002d471308c5598d036f0.pdf</ArchiveCopySource>
</Article>
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