Abstract
Two important aspects of tube-bundle boiling are examined experimentally, one relating to the form of heating, the other to the geometry. A 34-tube cell was constructed to test boiling under conditions of constant temperature and constant heat flux heating. The heat transfer under constant temperature conditions was 10% less. A 241-tube reboiler section was studied with in-line and staggered tube arrangements and the difference in heat transfer was found to be within experimental error. A simple equation reported previously is found to adequately correlate the results.
Original language | English |
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Title of host publication | Heat Transfer, Proceedings of the International Heat Transfer Conference |
Pages | 2137-2141 |
Number of pages | 5 |
Volume | 5 |
Publication status | Published - 1986 |