Hot water corrugated heat transfer tube
a heat transfer tube and corrugated technology, applied in tubular elements, corrosion prevention, coatings, etc., can solve the problems of increasing the pressure loss of the flow inside the tube, unable to achieve efficient heat exchange, etc., to prevent a reduction in the effect of heat transfer and reduce the heat transfer
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experiment 1
(1) Experiment 1
[0094]FIG. 5(a) is a cross sectional perspective view of the corrugated heat transfer tube 31. In Experiment 1, projections each having the height H1 are provided vertically symmetric on the tube inner surface having an inner diameter D of 8.0 mm in which the corrugated grooves 316 having a depth of Hm are provided. FIG. 5(b) is a cross sectional view taken along the A-A arrow in FIG. 5(a), and FIG. 5(c) is a cross sectional view taken along the B-B arrow in FIG. 5(b). As shown in FIG. 5(a) and FIG. 5(b), the projections 313 are formed on the inner surface by depressing the outer surface of the heat transfer tube. In addition, as shown in FIG. 5(c), each projection 313 is formed such that its shape in the transverse sectional view is elliptical. Here, flat surfaced parts 31a not provided with projections exist on the inner surface of the corrugated heat transfer tube 31.
[0095]FIG. 6(a) graphs, for each Reynolds number Re in the low Reynolds number section where the l...
experiment 2
(2) Experiment 2
[0097]To investigate the impact of the height H1 of the projections 313 on the heat transfer performance and on the pressure loss of the flow inside the tube, Experiment 2 was performed by varying the height H1 of the projections 313 provided on the tube inner surface. FIG. 7(a) graphs the heat transfer performance for the case where projections having differing heights H1 are provided vertically symmetric in a corrugated heat transfer tube having an inner diameter D of 8.0 mm such that the pitch P in the tube axial direction is 15 mm. Here, the horizontal axis represents the value of the height H1 of the projections 313. The vertical axis represents the ratio (Nu / Nuo), which is the ratio of the Nusselt number Nu of the corrugated heat transfer tube 31 provided with the projections 313 to the Nusselt number Nuo of the smooth tube not provided with projections. The solid line represents the experimental results for the case where the Reynolds number Re is 4,000, and t...
experiment 3
(3) Experiment 3
[0101]In Experiment 3, instead of assigning the height H1 of the projections 313, as is, as an index, the relative roughness (H1 / D) serves as the index. To investigate the impact of this relative roughness (H1 / D) on the heat transfer performance and on the pressure loss of the flow inside the tube, this experiment was performed by varying the relative roughness (H1 / D). FIG. 8(a) graphs the heat transfer performance of the corrugated heat transfer tube by varying the relative roughness (H1 / D) in the states when the Reynolds number Re is 2,000 and 4,000. Here, the horizontal axis represents the value of the relative roughness (H1 / D). The vertical axis represents the ratio (Nu / Nuo), which is the ratio of the Nusselt number Nu of the corrugated heat transfer tube 31 provided with the projections 313 to the Nusselt number Nuo of the smooth heat transfer tube not provided with projections. As shown in FIG. 8(a), the larger the value of the relative roughness (H1 / D) of the ...
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