Heat transfer in temperature-dependent non-Newtonian flow

dc.contributor.author	Wichterle, Kamil
dc.date.accessioned	2006-10-10T07:42:52Z
dc.date.available	2006-10-10T07:42:52Z
dc.date.issued	2004
dc.description.abstract	Flow and thermal convection in heat exchangers can be affected by variations in viscosity. In circular pipes the significance of this effect was expressed by Sieder and Tate’s empirical formula. Similar correction can be derived for other heat transfer problems. Exact solutions for heat transfer during the non-isoviscous laminar flow of Newtonian and non-Newtonian liquids in circular and flat ducts under conditions of constant wall temperature or constant wall heat flux are analyzed. Simple generalized procedures for heat transfer coefficient and friction estimate are recommended.	en
dc.identifier.citation	Chemical Engineering and Processing: Process Intensification. 2004, vol. 43, issue 10, p. 1223-1230.	en
dc.identifier.doi	10.1016/j.cep.2003.11.007
dc.identifier.issn	0255-2701
dc.identifier.location	Není ve fondu ÚK	en
dc.identifier.uri	http://hdl.handle.net/10084/56984
dc.identifier.wos	000224190200005
dc.language.iso	en	en
dc.publisher	Elsevier	en
dc.relation.ispartofseries	Chemical Engineering and Processing: Process Intensification	en
dc.relation.uri	http://dx.doi.org/10.1016/j.cep.2003.11.007	en
dc.subject	non-Newtonian flow	en
dc.subject	heat transfer coefficient	en
dc.subject	heat flux	en
dc.title	Heat transfer in temperature-dependent non-Newtonian flow	en
dc.type	article	en

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