8th Annual International Energy Conversion Engineering Conference 2010
DOI: 10.2514/6.2010-7087
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A Mass Computation Model for Light Weight Brayton Cycle Regenerator Heat Exchangers

Abstract: Based on a theoretical analysis of convective heat transfer across large internal surface areas, this paper discusses the design implications for generating lightweight gas-gas heat exchanger designs by packaging such areas into compact three-dimensional shapes. Allowances are made for hot and cold inlet and outlet headers for assembly of completed regenerator (or recuperator) heat exchanger units into closed cycle gas turbine flow ducting.Surface area and resulting volume and mass requirements are computed fo… Show more

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Cited by 8 publications
(6 citation statements)
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“…A 65 ppi, 25% dense foam has a higher specific area (∼6000 m 2 /m 3 compared to ∼3000 m 2 /m 3 ) than the best flat-plate heat exchangers and can operate at higher temperatures than most flat-plate joining allows [15]. They are also easier and less expensive to fabricate.…”
Section: Refractory Heat Exchangersmentioning
confidence: 94%
“…A 65 ppi, 25% dense foam has a higher specific area (∼6000 m 2 /m 3 compared to ∼3000 m 2 /m 3 ) than the best flat-plate heat exchangers and can operate at higher temperatures than most flat-plate joining allows [15]. They are also easier and less expensive to fabricate.…”
Section: Refractory Heat Exchangersmentioning
confidence: 94%
“…Power output for a given material mass was calculated, adding the thermoelectric material, the cold plate with water passage, and another plate with gas passage. The cost for the heat transfer section draws upon data for the mass per thermal resistance for both the hot-and cold-side plates [28]. Figure 13 shows the cost as a function of the flow rate of the working fluid.…”
Section: Cost Analysismentioning
confidence: 99%
“…Basic sizing data is needed for the heat exchanger for modelling its transient operation and for evaluating its weight, namely the characteristic length, area, volume and mass. These values are calculated according to the simplified method described by Juhasz [42] and adopting the values suggested by the author, specifically: heat transfer coefficient equal to 142 W/(m 2 K), density equal to 3900kg/m 3 and packing density of 3281m 2 /m 3 . The heat exchanger pressure drop at design point is assumed 4% for the cold side and 5% for the hot side including the exit duct losses, in line with the values suggested in [20].…”
Section: Recuperated Enginementioning
confidence: 99%