INTRODUKTIONIn the current energy crisis, the issue of energy efficiency of heat exchange processes and equipment for their provision in food, chemical, pharmaceutical, processing and other technologies becomes decisive. To increase the heat transfer coefficients in heat exchangers, various methods are used, in particular, the modification of the structural elements of boilers and other equipment [1], the increase in the turbulence of the refrigerant flows [2], the use of liquids with the optimal concentration of surfactants (SAS). For example, the maximum rate of heat exchange was observed when a nonionic surfactant was added to water [3]. The authors of [3] believed that the maximum rate of heat exchange in the first place may be due to the fact that this additive has a minimum capacity for the formation of foam. In addition, it is known that surfaceactive substances significantly, approximately 2 times, reduce the coefficients of surface tension of water and other liquids.
PROBLEM FORMULATIONAfter analyzing the literature sources, we came to the conclusion that the rate of heat exchange in liquid refrigerants through the laminar boundary layer (LBL) depends on the following main factors: -laminar flow is responsible for the turbulent flow, but is less energy-efficient [2,4]; -LBL, namely its average thickness is responsible for the total thermal resistance of the system [5,6]; -the thermal resistance depends on the coefficient of surface tension of the refrigerant [7]; -the intensity of heat exchange depends on the hydrophilicity or hydrophobicity of the wetting surface [8];Based on the foregoing, the purpose of this article was to offer a model for the interaction of refrigerants with a separating solid wall, which will cover all the above factors as much as possible. : 0392-8764 Vol. 35, No. 3, September 2017, pp. 678-682 DOI: 10.18280
INTERNATIONAL JOURNAL OF HEAT AND TECHNOLOGY
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ABSTRACTThe forces acting on the elementary volume of liquid in the pipeline in the laminar boundary layer are considered. A new dimensionless complex the surface number and the concept of the turbulence coefficient laminar boundary layer is proposed. The calculation of Froude, Euler numbers, the inverse Reynolds number and the surface number in laminar boundary layer for water under normal conditions is given. It is shown that the Froude number and the inverse Reynolds number are 4-5 orders of magnitude smaller than the surface number and Euler number in laminar boundary layer, which allows neglecting the forces of gravitation and friction in these conditions. Equations are proposed for calculating the average thickness of laminar boundary layer. The dependence of the surface number on the coefficient of surface tension of the refrigerant is obtained. It is shown that a decrease in the surface tension coefficient minimizes the average thickness of the laminar boundary layers in the wall system of the pipeline and liquid and increases the average velocities of the coolant flows in these layers, as a result of which such a s...