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105437 |
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|a Thiel, Gregory P.
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|a Massachusetts Institute of Technology. Department of Mechanical Engineering
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|a Rohsenow Kendall Heat Transfer Laboratory
|q (Massachusetts Institute of Technology)
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|a Lienhard, John H.
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|a Thiel, Gregory P.
|e contributor
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|a Lienhard, John H
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|a Lienhard, John H
|e author
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|a An Effectiveness--Number of Transfer Units Relationship for Evaporators With Non-negligible Boiling Point Elevation Increases
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|b American Society of Mechanical Engineers (ASME),
|c 2016-11-28T15:52:54Z.
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|z Get fulltext
|u http://hdl.handle.net/1721.1/105437
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|a An effectiveness number of transfer units (ε-NTU) model is developed for use in evaporators where the evaporating stream: (1) comprises a volatile solvent and nonvolatile solute(s) and (2) undergoes a significant, but linear change in boiling point elevation (BPE) with increasing solute molality. The model is applicable to evaporators driven by an isothermal stream (e.g., steam-driven or refrigerant-driven) in parallel flow, counterflow, and crossflow configurations where the evaporating stream is mixed. The model is of use in a variety of process engineering applications as well as the sizing and rating of evaporators in high-salinity desalination systems.
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|a King Fahd University of Petroleum and Minerals (Center for Clean Water and Clean Energy at MIT and KFUPM, project number R13-CW-10)
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|a en_US
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|a Article
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|t Journal of Heat Transfer
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