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Development of thermal sprayed tube and mesh heat exchangers for waste heat recovery

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Institution

http://id.loc.gov/authorities/names/n79058482

Degree Level

Master's

Degree

Master of Science

Department

Department of Mechanical Engineering

Supervisor / Co-Supervisor and Their Department(s)

Citation for Previous Publication

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Abstract

Development of a lab-scale heat exchanger with increased mesh to tube contact area was accomplished by flattening tubing prior to attaching wire mesh. This novel heat exchanger prototype utilizes thermal sprayed coating to attach wire mesh onto tubing surfaces instead of conventional brazing or welding of extended surfaces. Twin wire arc spray equipment was utilized to deposit stainless steel coating onto stainless steel mesh and tube. Four samples with varied coating thicknesses and spray deposition settings were fabricated to be compared with an unmeshed sample to quantify the heat transfer enhancement of the mesh.

A simple heated wind tunnel was designed in tandem with the lab scale prototype. Air propelled by axial fan towards the sample placed inside a rectangular duct, is heated by a propane torch, mimicking the environment at the exhaust of flare or flue gas stacks. Steady state inlet and outlet water temperatures were measured. For heat transferred into the water, meshed and coated samples performed 38% to 217% better than bare tube. Temperature difference trends were in line with previous studies but magnitudes were 1.5 to 4 times greater, demonstrating the heat transfer enhancement from wire mesh, flattened tube, and thicker coatings.

A fin model is developed to quantify the heat transfer from mesh wires and integrated into a discretized energy balance to predict outlet temperatures a priori and quantify thermal resistances in each sample. The results of the model indicate that coating thickness has the largest impact on thermal resistance, with values at least 1 or 2 orders of magnitude greater than other thermal resistances in the heat transfer network of the lab scale meshed tubular heat exchangers. The fin temperature distribution also exhibits small lengths of temperature variation along the fin, meaning future designs need not utilize fins longer than 4 mm, showing potential reductions in material, weight and size without impacting performance.

Item Type

http://purl.org/coar/resource_type/c_46ec

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Permission is hereby granted to the University of Alberta Libraries to reproduce single copies of this thesis and to lend or sell such copies for private, scholarly or scientific research purposes only. Where the thesis is converted to, or otherwise made available in digital form, the University of Alberta will advise potential users of the thesis of these terms. The author reserves all other publication and other rights in association with the copyright in the thesis and, except as herein before provided, neither the thesis nor any substantial portion thereof may be printed or otherwise reproduced in any material form whatsoever without the author's prior written permission.

Language

en

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