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Compact Tube and Plate-Finned Heat Exchangers
A highly effective method for heat transfer enhancement in tube and plate-finned heat exchangers through artificial flow turbulization is proposed. Heat transfer surfaces of different design and their production are developed. A correlation for the increase in heat transfer is found as a function of...
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Published in: | Heat transfer engineering 1985-01, Vol.6 (1), p.44-51 |
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container_end_page | 51 |
container_issue | 1 |
container_start_page | 44 |
container_title | Heat transfer engineering |
container_volume | 6 |
creator | KALININ, ELWIN KONSTANTINOVICH DREITSER, GENRIKH ALEKSANDROVICH DUBROVSKY, EUGENII VLADIMIROVICH |
description | A highly effective method for heat transfer enhancement in tube and plate-finned heat exchangers through artificial flow turbulization is proposed. Heat transfer surfaces of different design and their production are developed. A correlation for the increase in heat transfer is found as a function of increasing hydraulic resistance for channels of various cross sections. Results are compared with similar smooth channels with discrete wall flow turbulization. The use of the proposed surfaces allows a 1.5- to 2-fold decrease in the heat exchanger volume, a 3- to 8-fold increase in film boiling heat transfer, a 1.4-fold increase in surface boiling heat transfer, and a 2- to 3.4-fold increase in condensation heat transfer on the outer surfaces of annular grooved tubes as well as a decrease in the salt deposition on the outer and inner surfaces of tubes. |
doi_str_mv | 10.1080/01457638508939618 |
format | article |
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Heat transfer surfaces of different design and their production are developed. A correlation for the increase in heat transfer is found as a function of increasing hydraulic resistance for channels of various cross sections. Results are compared with similar smooth channels with discrete wall flow turbulization. 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Heat transfer surfaces of different design and their production are developed. A correlation for the increase in heat transfer is found as a function of increasing hydraulic resistance for channels of various cross sections. Results are compared with similar smooth channels with discrete wall flow turbulization. The use of the proposed surfaces allows a 1.5- to 2-fold decrease in the heat exchanger volume, a 3- to 8-fold increase in film boiling heat transfer, a 1.4-fold increase in surface boiling heat transfer, and a 2- to 3.4-fold increase in condensation heat transfer on the outer surfaces of annular grooved tubes as well as a decrease in the salt deposition on the outer and inner surfaces of tubes.</abstract><pub>Taylor & Francis Group</pub><doi>10.1080/01457638508939618</doi><tpages>8</tpages></addata></record> |
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ispartof | Heat transfer engineering, 1985-01, Vol.6 (1), p.44-51 |
issn | 0145-7632 1521-0537 |
language | eng |
recordid | cdi_crossref_primary_10_1080_01457638508939618 |
source | Taylor & Francis Engineering, Computing & Technology Archive |
subjects | channels flow heat exchangers surface properties tubes |
title | Compact Tube and Plate-Finned Heat Exchangers |
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