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Heat transfer to newtonian and inelastic non-newtonian fluids flowing across tube banks

dc.contributor.authorPrakash O.; Gupta S.N.
dc.date.accessioned2025-05-24T09:58:05Z
dc.description.abstractHeat transfer coefficients are measured with water and 1.0-4.0% aqueous carboxymethylcellulose solutions flowing across a tube bank with a triangular pilch of 1.43 cm and a 1.50 pitch ratio. A parallel-plate channel model is used to define the flow in the bank. Based on this model a single-valued correlation is proposed for both Newtonian and inelastic non-Newtonian fluids. © 1987 Taylor and Francis Group, LLC.
dc.identifier.doihttps://doi.org/10.1080/01457638708962783
dc.identifier.urihttp://172.23.0.11:4000/handle/123456789/22898
dc.relation.ispartofseriesHeat Transfer Engineering
dc.titleHeat transfer to newtonian and inelastic non-newtonian fluids flowing across tube banks

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