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Momentum Transfer in Curved Pipes. 2. Non-Newtonian Fluids

P. Mishra, +1 more
- 01 Jan 1979 - 
- Vol. 18, Iss: 1, pp 130-137
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This article is published in Industrial & Engineering Chemistry Process Design and Development.The article was published on 1979-01-01. It has received 257 citations till now. The article focuses on the topics: Momentum diffusion & Momentum transfer.

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A review of flow and heat transfer characteristics in curved tubes

TL;DR: In this paper, a literature review on heat transfer and flow characteristics of single-phase and two-phase flow in curved tubes is presented, where three main categories of curved tubes; helically coiled tubes, spirally coiling tubes, and other coiled tube, are described.
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A Review on the Potential Applications of Curved Geometries in Process Industry

TL;DR: The potential industrial applications of curved tubes for single and two-phase flow are reviewed within the context of physics of flow, trends in the development of technology, and its laboratory to industrial-scale commercialization.
Journal ArticleDOI

Pressure drop and heat transfer study in tube-in-tube helical heat exchanger

TL;DR: In this paper, the authors investigated the hydrodynamics and heat transfer characteristics of tube-in-tube helical heat exchanger at the pilot plant scale, where the inner and outer tubes were fitted with semicircular plates to support the inner tube and provide high turbulence in the annulus region.
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Numerical study on turbulent heat transfer and pressure drop of nanofluid in coiled tube-in-tube heat exchangers

TL;DR: In this paper, a computational fluid dynamics (CFD) study has been carried out to study the heat transfer and pressure drop characteristics of water-based Al 2 O 3 nanofluid flowing inside coiled tube-in-tube heat exchangers.
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Fully developed laminar flow in a helically coiled tube of finite pitch

TL;DR: In this paper, a solution for steady, fully developed, laminar flow of an incompressible Newtonian fluid through a helically coiled tube of finite pitch was obtained by finite difference calculations.