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The compact plate reactor and test system were designed to match the new catalyst.
The condenser, evaporator and solution heat exchanger are compact plate heat exchangers.
The objective is to propose a tool for computer aided design of compact plate fin heat exchangers.
The article presents a novel compact plate finned-tube air-fuel heat exchanger which is designed by means of using logarithmic mean temperature difference method (LMTD) and both thermal and hydraulic performance of the heat exchanger are experimentally investigated.
In particular for compact plate heat exchangers, the overall heat transfer coefficient strongly varies with the manufacturer's plate design and has to be identified by means of extensive measurements.
The steam reforming performance of Cu-Ni and Cu-Ni-Fe catalysts and the hydrogen production capacity of the compact plate reactor were investigated at different temperatures and gas hourly space velocity (GHSV) using dimethyl ether (DME) as the feedstock.
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The system is designed as thermoelectric generators (TEGs) sandwiched in the walls of a compact plate-fin heat exchanger.
A compact plate-fin reformer (PFR) consisting of closely spaced plate-fins, in which endothermic and exothermic reactions take place in alternate chambers, has been studied.
Three offset strip fin and 16 wavy fin geometries used in the compact plate-fin heat exchangers have also been analyzed numerically.
Three typical compact plate-fin heat exchangers have been analyzed using Fluent software for quantification of flow maldistribution effects with ideal and real cases.
Efficient and compact plate-fin heat exchangers are critical for large-scale helium liquefaction/refrigeration systems as they constitute major part in the cold box.
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