Experimental Investigation on Hydrodynamic and Thermal Performance of a Gas-Liquid Thermosyphon Heat Exchanger in a Pilot Plant

Waste heat recovery is very important, because not only it reduces the expenditure of heat generation, but also it is of high priority in environmental consideration, such as reduction in greenhouse gases. One of the devices is used in waste heat recovery is heat pipe heat exchanger.Anexperimental research has been carried out to investigate the hydrodynamic and thermal performance of a gas- liquid thermosyphon heat exchanger “THE” in a pilot plant. The ε-NTU method has been used. The pressure drop has been calculated across tube bundle of the thermosyphon heat exchanger. It's module is composed of ۶ “rows” and ۱۵ “columns” copper pipes with aluminum plate fins with dimensions of ۱۳۰ cm “height”, ۴۷ cm “width” and  ۲۰ cm “depth” . The tubes have been filled by water with filling ratio of ۳۰ %, ۵۰ % and ۷۰ %. The density and thickness of fins are ۳۰۰ fin/m and ۰.۴ mm, respectively. The configuration of tubes is in-line with ۳۰ mm pitch. The results show that as the ratio of Ce/Cc raises the amount of heat transfer increases. The effectiveness of heat pipe heat exchanger remains constant as the temperature of hot stream rises, but the amount of heat transfer increases. Filling ratio in normal region (۳۰-۷۰ %) has no effects on experimental results. A new correlation for thermosyphon heat exchanger with individual finned tubes and in-line geometry has been proposed for calculating pressure drop across tube bank of a “THE”. The error in pressure drop for ۴۰ experimental points in the new correlation is less than ۱۵ %. This indicates that the new correlation possesses an acceptable accuracy predicting pressure drop.

کلیدواژه ها:

Thermosyphon heat exchanger "THE" ، ε-NTU method ، in-line configuration ، Pressure drop ، Finned tube bundle