As a result,the heat balance deviations of two sides' water were no more than 10 percent. Experimental turbulent flow heat transfer Nusselt numbers agreed with the predicted values within 10%. Accordingly,the system is reliable to be used to monitor the fouling process of heat transfer surface
This thesis first research the effect of the additive and material, which can restrain ice crystal adhere onto the heat exchange surface. Then oriented at practical industrial application, a new kind of shell and tube type dynamic ice generator is designed.
A finned tube is the key component of a finned tube heat exchanger, and the fin efficiency is one of the main parameters in designing a finned tube heat exchanger, and it also has certain applicable value in the comparison of heat exchange surface.
Method and formulae for calculating the mean forced convection heat-transfer coefficient of the blade surface,as well as for the blade passage's bottom wall,are introduced.
Experimentally found local heat transfer coefficients are analyzed as a function of the measuring point on the heat transfer surface area of the agitated vessel wall and of the impeller eccentricity.
Theoretical formulas are obtained for determining the heat transfer surface of a regenerator in the case of the heat capacity of one of the heat transfer fluids, and also the heat transfer coefficient varying substantially through the equipment.
With the aid of an interferometer, the dependence of heat transfer coefficient in unsteady heat transfer on the rate of change of thermal stress at the heat transfer surface has been determined.
It is also shown that the decline in the measured temperatures of circulation fluids since 1985 to the present is consistent with the heat exchange surface area going through a maximum in 1987.
It is shown that the true value of the average temperature depends on the geometry of the heat transfer surfaces and is less than the arithmetic mean value usually employed.
Heat rejection rates from a plate-fin tube type condenser are determined for various flow rates and inlet state conditions of air and for different degrees of wetting of the heat transfer surfaces.
Consequently, the heat transfer coefficient shows a significant increase for α>amp;gt;0.4, suggesting an excellent performance of heat transfer surfaces in the duct of cross-shaped cross-section.
In order to simplify the design program, of a plate-fin heat exchanger, a more efficient method is suggested for evaluating the behavior of the plate fins so that optimum could be achieved in selecting surfaces of a heat exchanger.In addition, thermodynimic analysis is made of the operation of a plate-fin heat exchanger and a mathematical model is built for investigating its en-tropy change and production, thus providing new means for improving a heat exchanger.
A technical and economical analysis for making optimized selection of heat transfer tubes was proposed in the article based on the heat transfer and pressure drop characteristics of three different types of tubes of domestic design. As shown by the results, heat transfer tubes with extended surface can only be widely used under a reasonable price calculated through technical and economical analysis.
The performance for the boiling heat transfer of the machined porous tube bundle has been theoretically analysed and experimentally studied,The results show that the performance of the tube bundle is different from that of a single tube,and it is not the same either in different place of the same tube,and the nature and magnitudes of the differences depond on the density heat flux and tube structure of the bundle.Dividing the surface of the tube into three parts to be analyzed,it will give a perfect explana...