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eng Newell, Ty A. Hurlburt, Evan Timothy 2015-09-25T21:12:53Z 2015-09-25T21:12:53Z 10000-01-01 1997 1997 The model demonstrates the mechanisms which cause circumferential and axial composition and temperature gradients in the liquid film when zeotropic mixtures undergo evaporation and condensation. Heat transfer in mixtures is shown to be less than the ideal limit due to mass transfer resistance in the vapor. The mass transfer resistance causes bulk temperatures to differ from equilibrium bulk temperatures thus decreasing the temperature difference which drives heat transfer. Made available in DSpace on 2015-09-25T21:12:53Z (GMT). No. of bitstreams: 2 license.txt: 4848 bytes, checksum: 96035ab3f5e1c23cc7138a224ce498bd (MD5) 9812636.pdf: 8546915 bytes, checksum: ab7d316f3807106eb46c7293fe4469c6 (MD5) Previous issue date: 1997 Embargo set by: Seth Robbins for item 85235 Lift date: Forever Reason: Restricted to the U of I community idenfinitely during batch ingest of legacy ETDs Restricted to the U of I community idenfinitely during batch ingest of legacy ETDs U of I Only 54 p. Thesis (Ph.D.)--University of Illinois at Urbana-Champaign, 1997. http://hdl.handle.net/2142/83954 (MiAaPQ)AAI9812636 Engineering, Mechanical Modeling of the Evaporation and Condensation of Zeotropic Refrigerant Mixtures in Horizontal Annular Flow text Mechanical Engineering Mechanical Engineering University of Illinois at Urbana-Champaign Dissertation Ph.D.