2018
DOI: 10.3390/en11113044
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Thermo-Economic Analysis of a Bottoming Kalina Cycle for Internal Combustion Engine Exhaust Heat Recovery

Abstract: The use of a Kalina cycle (KC) with a superheater to recover waste heat from an internal combustion engine (ICE) is described in this paper. The thermodynamic and economic analyses are performed for KC. The results indicate that using KC with a superheater is a feasible method to recover waste heat from ICE. The maximum thermal efficiency of KC is 46.94% at 100% ICE percentage load. The improvement of thermal efficiency is greater than 10% at all ICE loads, and the maximum improvement of thermal efficiency is … Show more

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Cited by 10 publications
(1 citation statement)
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“…In the heat exchanger cost equation, 𝐴 β„Žπ‘₯ is the amount of heat transfer area, which is obtained by dividing the heat capacity of each exchanger by the heat transfer coefficient, which according to the reference [32] for the evaporator 1.1(π‘˜π‘Š π‘š 2 𝐾 ⁄ ) , for recuperator 0.7(π‘˜π‘Š π‘š 2 𝐾 ⁄ )and for condensers 0.5(π‘˜π‘Š π‘š 2 𝐾 ⁄ ). 𝑓 π‘‘π‘’π‘šπ‘ and 𝑓 π‘π‘Ÿπ‘’π‘  are temperature correction coefficient and pressure correction coefficient, respectively, obtained from the reference [33] according to the characteristics of the heat exchanger.…”
Section: Γ— 𝑓 π‘π‘Ÿπ‘’π‘  Γ— 𝑓 π‘‘π‘’π‘šπ‘mentioning
confidence: 99%
“…In the heat exchanger cost equation, 𝐴 β„Žπ‘₯ is the amount of heat transfer area, which is obtained by dividing the heat capacity of each exchanger by the heat transfer coefficient, which according to the reference [32] for the evaporator 1.1(π‘˜π‘Š π‘š 2 𝐾 ⁄ ) , for recuperator 0.7(π‘˜π‘Š π‘š 2 𝐾 ⁄ )and for condensers 0.5(π‘˜π‘Š π‘š 2 𝐾 ⁄ ). 𝑓 π‘‘π‘’π‘šπ‘ and 𝑓 π‘π‘Ÿπ‘’π‘  are temperature correction coefficient and pressure correction coefficient, respectively, obtained from the reference [33] according to the characteristics of the heat exchanger.…”
Section: Γ— 𝑓 π‘π‘Ÿπ‘’π‘  Γ— 𝑓 π‘‘π‘’π‘šπ‘mentioning
confidence: 99%