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Date of download: 9/16/2016 Copyright © ASME. All rights reserved. From: Evaluation of Heat and Mass Transfer Models for Sizing Low-Temperature Kalina.

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Presentation on theme: "Date of download: 9/16/2016 Copyright © ASME. All rights reserved. From: Evaluation of Heat and Mass Transfer Models for Sizing Low-Temperature Kalina."— Presentation transcript:

1 Date of download: 9/16/2016 Copyright © ASME. All rights reserved. From: Evaluation of Heat and Mass Transfer Models for Sizing Low-Temperature Kalina Cycle Microchannel Condensers J. Energy Resour. Technol. 2016;139(2):022002-022002-10. doi:10.1115/1.4034229 Kalina cycle schematic Figure Legend:

2 Date of download: 9/16/2016 Copyright © ASME. All rights reserved. From: Evaluation of Heat and Mass Transfer Models for Sizing Low-Temperature Kalina Cycle Microchannel Condensers J. Energy Resour. Technol. 2016;139(2):022002-022002-10. doi:10.1115/1.4034229 Schematic of coupled heat and mass transfer resistances during zeotropic condensation Figure Legend:

3 Date of download: 9/16/2016 Copyright © ASME. All rights reserved. From: Evaluation of Heat and Mass Transfer Models for Sizing Low-Temperature Kalina Cycle Microchannel Condensers J. Energy Resour. Technol. 2016;139(2):022002-022002-10. doi:10.1115/1.4034229 Kalina cycle simulated efficiency versus bulk ammonia mass fraction at different evaporator pressures Figure Legend:

4 Date of download: 9/16/2016 Copyright © ASME. All rights reserved. From: Evaluation of Heat and Mass Transfer Models for Sizing Low-Temperature Kalina Cycle Microchannel Condensers J. Energy Resour. Technol. 2016;139(2):022002-022002-10. doi:10.1115/1.4034229 Schematic of (a) single microchannel heat exchanger slab and (b) concept of multislab microchannel heat exchanger Figure Legend:

5 Date of download: 9/16/2016 Copyright © ASME. All rights reserved. From: Evaluation of Heat and Mass Transfer Models for Sizing Low-Temperature Kalina Cycle Microchannel Condensers J. Energy Resour. Technol. 2016;139(2):022002-022002-10. doi:10.1115/1.4034229 Schematic of segmented model Figure Legend:

6 Date of download: 9/16/2016 Copyright © ASME. All rights reserved. From: Evaluation of Heat and Mass Transfer Models for Sizing Low-Temperature Kalina Cycle Microchannel Condensers J. Energy Resour. Technol. 2016;139(2):022002-022002-10. doi:10.1115/1.4034229 Nonequilibrium model inputs and outputs Figure Legend:

7 Date of download: 9/16/2016 Copyright © ASME. All rights reserved. From: Evaluation of Heat and Mass Transfer Models for Sizing Low-Temperature Kalina Cycle Microchannel Condensers J. Energy Resour. Technol. 2016;139(2):022002-022002-10. doi:10.1115/1.4034229 Heat exchanger area versus condensation modeling approach Figure Legend:

8 Date of download: 9/16/2016 Copyright © ASME. All rights reserved. From: Evaluation of Heat and Mass Transfer Models for Sizing Low-Temperature Kalina Cycle Microchannel Condensers J. Energy Resour. Technol. 2016;139(2):022002-022002-10. doi:10.1115/1.4034229 Comparison of (a) Fronk and Garimella [39] heat transfer coefficient with and without Silver–Bell–Ghaly correction factor and (b) local heat flux of nonequilibrium and equilibrium condenser design model Figure Legend:


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