BRIEF DESCRIPTION OF THE DRAWINGS
The preferred embodiments according to the invention will be explained below referring to the drawings, wherein:
FIG. 1A is an explanatory diagram of an entire view showing structure of a heat transfer tube in a first preferred embodiment according to the present invention;
FIG. 1B is an enlarged cross-sectional view in region A of FIG. 1A;
FIG. 2 is an explanatory diagram showing structure of a heat transfer tube in a second preferred embodiment according to the present invention;
FIG. 3 is an explanatory diagram showing structure of a heat exchanger in a third preferred embodiment according to the present invention;
FIG. 4 is an explanatory diagram showing structure of a heat exchanger in a fourth preferred embodiment according to the present invention;
FIG. 5 is an explanatory diagram showing structure of a heat exchanger in a fifth preferred embodiment according to the present invention;
FIG. 6 is an explanatory diagram showing structure of a heat exchanger in a sixth preferred embodiment according to the present invention;
FIG. 7 is an explanatory diagram showing structure of a heat exchanger in a seventh preferred embodiment according to the present invention;
FIG. 8 is a diagram showing the comparison of heat transfer performance of the corrugated heat transfer tube of the first embodiment (example 1), of a plain tube (comparison example 1), and of an inner-grooved tube (comparison example 2);
FIG. 9 is a diagram showing the relationship between Hc/OD and heat transfer performance of the corrugated heat transfer tube, i.e., heat transfer performance ratio relative to a plain tube for Reynolds number Re=1000;
FIG. 10 is a diagram showing the relationship between twist angle βc and heat transfer performance of the corrugated heat transfer tube, i.e., heat transfer performance ratio relative to a plain tube for Reynolds number Re=1000; and
FIG. 11 is a diagram showing the relationship between Hc/OD and friction coefficient of the corrugated heat transfer tube, i.e., tube friction coefficient ratio relative to a plain tube for Reynolds number Re=1000.