Shell-and-tube heat exchangers are widely used in various industries for heating or cooling one of the heat carriers to the required temperature value. The key criterion for the performance of such heat exchangers is the ability to ensure continuous heat exchange between the heat carriers both in the absence of the possibility of heat carrier leaks into the external environment and in the absence of the possibility of mixing the heat carriers. One of the most common causes of failure of shell-and-tube heat exchangers during operation is a violation of the separation of the cooling and cooled media due to the destruction of the pipe wall due to mechanical and temperature stresses, which necessitates the study of methods aimed at reducing stresses caused by uneven temperature distribution in the structural elements. The paper considers a method for reducing stresses caused by uneven temperature distribution across the tube thickness in a heat exchanger by adding a smaller diameter tube into the main coil tube. Comparative analysis is performed for heat exchanger designs without an insert in the coil, as well as a design with the introduction of an internal tube of a smaller diameter at the initial section of the coil. During the comparative analysis, an assessment is made of the effect of the modified design on the heat exchange and strength characteristics of the heat exchanger. A theoretical description of the proposed method is given based on the fourth theory of strength, as well as a mathematical model of a computational experiment of the heat exchanger operation, including the Navier-Stokes equation and heat transfer equation and description of the behavior of a solid deformable body with a linear isotropic model of the material in the elastic zone. Based on the results of the computational experiment of the heat exchanger operation process, it is shown that the use of the flow separation method does not have a significant effect on the thermal-hydraulic characteristics of the heat exchanger, reducing the values of thermal expansion in the structure, and thereby reducing the stresses that arise in the inlet pipe of the coil, which increases the strength and service life of the structure, thereby increasing the service life of the heat exchanger.
Vargaftik NB. Handbook of Thermophysical Properties of Gases and Liquids. Fizmatgiz; 1963, 708 p. (In Russ).
Shteinberg MO. (3rd. ed.). Handbook of Hydraulic Resistances. Mechanical Engineering; 1992. 662 p. (In Russ).
Andreev PA, Gremilov DI, Fedorovich ED. (2nd ed.). Heat Exchangers of Nuclear Power Plants. Sudostroenie. 1969. 352 p. (In Russ).
Birger IA, Shorr BF, Iosilevich GB. (3rd ed.). Strength Calculation of Machine Parts. Mechanical Engineering; 1979. 702 p. (In Russ).
Altshul AD. (2nd ed.). Hydraulic Resistances. NEDRA; 1982. 224 p. (In Russ).
Loitsyanskii LG. Mechanics of liquid and gas. Moscow: Drofa; 2003. 846 p. (In Russ).
Anikeev AA, Molchanov AM, Yanyshev DS. Fundamentals of computational heat transfer and hydrodynamics. Moscow: MAI; 2010. 149 p. (In Russ).
PNAE G-7-002-86 Standards for calculating the strength of equipment and pipelines of nuclear power plants. Energoatomizdat; 1989. 525 p. (In Russ).
Abramovich GN. Theory of turbulent jets. Moscow: State Publishing House of Physical and Mathematical Literature; 1960. 715 p. (In Russ).
Lebedev NN. Temperature stresses in the theory of elasticity. Moscow Leningrad: ONTI. Main editorial office of technical and theoretical literature; 1937. 110 p. (In Russ).
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