| Autor: |
Zakharov, V. P., Minsker, K. S., Berlin, Al. Al., Shevlyakov, F. B. |
| Předmět: |
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| Zdroj: |
Theoretical Foundations of Chemical Engineering; Sep/Oct2004, Vol. 38 Issue 5, p499-502, 4p |
| Abstrakt: |
The heat-transfer coefficient in a divergent–convergent tubular apparatus is 1.4–1.7 times larger than that in a cylindrical apparatus, the specific output of the divergent–convergent tubular apparatus is 1.3–1.4 times higher than that of the cylindrical apparatus, and the residence time of a reaction mixture (or a heat-transfer medium) in the heat-transfer zone of the divergent–convergent tubular apparatus is 1.8 times shorter than that of the cylindrical apparatus. A relationship is revealed between the heat-transfer coefficient and the liquid flow pattern. [ABSTRACT FROM AUTHOR] |
| Databáze: |
Complementary Index |
| Externí odkaz: |
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