Prediction of Shell Side Heat Transfer Coefficient for Common Gases

Please use this identifier to cite or link to this item: http://hdl.handle.net/2080/981

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DC Field	Value	Language
dc.contributor.author	Swain, Anup Kumar	-
dc.contributor.author	Roy, G K	-
dc.date.accessioned	2009-08-03T09:39:31Z	-
dc.date.available	2009-08-03T09:39:31Z	-
dc.date.issued	2004	-
dc.identifier.citation	Chemical Engineering World , August 2004	en
dc.identifier.uri	http://hdl.handle.net/2080/981	-
dc.description.abstract	Empirical relations are available for the calculation of heat transfer coefficient for the shell side fluid. However, most widely adopted method by the designers is the vs. Reynolds Number plot presented by Kern[1]. This is used for the hydrocarbons, organic compounds, water, aqueous solutions and gases. The above relation between jH and Reynolds	en
dc.format.extent	239882 bytes	-
dc.format.mimetype	application/pdf	-
dc.language.iso	en	-
dc.title	Prediction of Shell Side Heat Transfer Coefficient for Common Gases	en
dc.type	Article	en
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