Numerical results of falling film absorption with water-ammonia.
Author(s) : WASSENAAR R. H., SEGAL A.
Summary
A model was set up for the heat, mass and momentum transport in a falling film absorber with a binary gas phase. Results are given for water-ammonia and countercurrent gas flow. If the ratio of diffusion to convection is not negligible (here for a gas channel smaller than 5 millimeters), absorption is higher with countercurrent gas flow than with cocurrent flow. For larger gas channels the outcomes from a simpler one-component gas phase model are, if the interface boundary conditions are formulated correctly, almost equal to the outcomes from the presented model.
Details
- Original title: Numerical results of falling film absorption with water-ammonia.
- Record ID : 1999-3557
- Languages: English
- Source: Thermodynamics, heat and mass transfer of refrigeration machines and heat pumps. Proceedings of the EUROTHERM Seminar 59./ Thermodynamique et transferts de chaleur et de masse dans les machines à froid et pompes à chaleur. Comptes rendus du séminaire EUROTHERM 59.
- Publication date: 1998/07/06
- Document available for consultation in the library of the IIR headquarters only.
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Indexing
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- Source: ASHRAE Transactions. 2001 Winter Meeting, Atlanta, GA. Volume 107, part 1 + CD-ROM.
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- Date : 1999/03/24
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- Source: Proceedings of the International Sorption Heat Pump Conference.
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- Formats : PDF
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- Source: 7th IIR-Gustav Lorentzen Conference on Natural Working Fluids (GL2006). Proceedings
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