The direct heat exchange network (direct flow mixing network) and the indirect heat exchange network (exchanger network) are two of the elements that constitute a water network where heat and mass are transferred. When designing these systems, it is important to consider different aspects such as thermodynamics and equipment costs. This paper analyzes different design options within the framework of heuristic methodologies on a case study taken from the open literature. Two design methodologies are compared on the basis of exergy losses. It also enunciates a series of considerations in heuristic design for the heat and mass exchange networks. A very helpful tool in relation with the considerations set out herein is the composite curve; special focus will be given during its construction. This paper shows how to incorporate the exergy component in design seeking to minimize the thermal irreversibility.
Thermodynamic Analysis of Simultaneous Heat and Mass Transfer Systems
Contributed by the Advanced Energy Systems Division of ASME for publication in the JOURNAL OF ENERGY RESOURCES TECHNOLOGY. Manuscript received October 26, 2015; final manuscript received June 21, 2016; published online July 25, 2016. Assoc. Editor: Alojz Poredos.
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Martinez-Patiño, J., Serra, L., Verda, V., Picón-Núñez, M., and Rubio-Maya, C. (July 25, 2016). "Thermodynamic Analysis of Simultaneous Heat and Mass Transfer Systems." ASME. J. Energy Resour. Technol. November 2016; 138(6): 062006. https://doi.org/10.1115/1.4034068
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