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Final Report Modifications and Optimization of the Organic Rankine Cycle to Improve the Recovery of Waste Heat

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Final Report Modifications and Optimization of the Organic Rankine Cycle to Improve the Recovery of Waste Heat ( final-report-modifications-and-optimization-organic-rankine- )

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Economizer Evaporator Superheater Figure 17. Working fluid side surface temperature in direct evaporators. 2.3.3 Heat Exchanger Design Summary The preliminary design of the boiler includes three harps of fin tube bundles, economizer, superheater, and evaporator, suspended in a rectangular duct. The number of rows is 24, 2, and 2, respectively, to give a total of 28 with 60 tubes per row. The economizer section only has two rows per pass for lower pressure loss; economizer and superheater are in counterflow to the exhaust gas and the two evaporator rows are arranged in parallel flow. The headers are laid out as manifolds on top of the tube bundles, with each bundle having a once-through flow path. The headers are tentatively placed outside the duct to prevent having zones of hot, slow moving fluid near walls and headers with weld seams, in which in case of a leak the risk of autoignition could increase. A simple schematic of the direct evaporator design is shown in Figure 18. 17

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