11 research outputs found
Mathematical modeling heat transfer in closed two-phase thermosyphon
ΠΡΠΎΠ²Π΅Π΄Π΅Π½ ΡΠΈΡΠ»Π΅Π½Π½ΡΠΉ Π°Π½Π°Π»ΠΈΠ· ΡΠ΅ΠΏΠ»ΠΎΠΏΠ΅ΡΠ΅Π½ΠΎΡΠ° Π² Π·Π°ΠΌΠΊΠ½ΡΡΠΎΠΌ Π΄Π²ΡΡ
ΡΠ°Π·Π½ΠΎΠΌ ΡΠ΅ΡΠΌΠΎΡΠΈΡΠΎΠ½Π΅ ΡΠΈΠ»ΠΈΠ½Π΄ΡΠΈΡΠ΅ΡΠΊΠΎΠΉ ΡΠΎΡΠΌΡ Π² ΡΡΠ»ΠΎΠ²ΠΈΠΈ ΠΏΠΎΠ΄Π²ΠΎΠ΄Π° ΡΠ΅ΠΏΠ»ΠΎΡΡ Π½Π° Π½ΠΈΠΆΠ½Π΅ΠΉ ΠΊΡΡΡΠΊΠ΅. ΠΠ»Ρ ΠΎΠΏΠΈΡΠ°Π½ΠΈΡ ΠΈΡΡΠ»Π΅Π΄ΡΠ΅ΠΌΠΎΠ³ΠΎ ΠΏΡΠΎΡΠ΅ΡΡΠ° ΠΏΡΠ΅Π΄Π»ΠΎΠΆΠ΅Π½Π° ΡΠΏΡΠΎΡΠ΅Π½Π½Π°Ρ ΠΌΠ°ΡΠ΅ΠΌΠ°ΡΠΈΡΠ΅ΡΠΊΠ°Ρ ΠΌΠΎΠ΄Π΅Π»Ρ, ΠΎΡΠ»ΠΈΡΠ°ΡΡΠ°ΡΡΡ ΠΎΡ ΠΈΠ·Π²Π΅ΡΡΠ½ΠΎΠΉ ΠΎΠΏΠΈΡΠ°Π½ΠΈΠ΅ΠΌ ΡΠΎΠ»ΡΠΊΠΎ ΠΏΡΠΎΡΠ΅ΡΡΠΎΠ² ΡΠ΅ΠΏΠ»ΠΎΠΏΡΠΎΠ²ΠΎΠ΄Π½ΠΎΡΡΠΈ Π² ΡΠΈΡΡΠ΅ΠΌΠ΅ "ΠΊΠΎΡΠΏΡΡ ΡΠ΅ΡΠΌΠΎΡΠΈΡΠΎΠ½Π° - ΠΏΠ°ΡΠΎΠ²ΠΎΠΉ ΠΊΠ°Π½Π°Π» - ΠΏΠ»Π΅Π½ΠΊΠ° ΠΊΠΎΠ½Π΄Π΅Π½ΡΠ°ΡΠ°". Π‘ΡΠΎΡΠΌΡΠ»ΠΈΡΠΎΠ²Π°Π½Π½Π°Ρ ΠΊΡΠ°Π΅Π²Π°Ρ Π·Π°Π΄Π°ΡΠ° ΡΠ΅ΡΠ΅Π½Π° ΠΌΠ΅ΡΠΎΠ΄ΠΎΠΌ ΠΊΠΎΠ½Π΅ΡΠ½ΡΡ
ΡΠ°Π·Π½ΠΎΡΡΠ΅ΠΉ. ΠΠΎΠ»ΡΡΠ΅Π½Ρ ΠΏΠΎΠ»Ρ ΡΠ΅ΠΌΠΏΠ΅ΡΠ°ΡΡΡ Π² ΡΠ΅ΡΠΌΠΎΡΠΈΡΠΎΠ½Π΅ Π΄Π»Ρ ΡΠΈΠΏΠΈΡΠ½ΡΡ
ΡΠ΅ΠΏΠ»ΠΎΠ²ΡΡ
Π½Π°Π³ΡΡΠ·ΠΎΠΊ ΠΈ ΡΠ΅ΠΆΠΈΠΌΠΎΠ² ΡΠ°Π±ΠΎΡΡ
The Opportunity Analyses of Using Thermosyphons in Cooling Systems of Power Transformers on Thermal Stations
The opportunity analyses of using the thermosyphons as the main elements in the systems of thermal regime supplying has been conducted under the conditions of their usage in power transformers on thermal stations. Mathematical modeling of jointly proceeding processes of conduction, forced convection and phase transitions (evaporation and condensation) of coolant in the thermosyphon of rectangular cross section has been carried out. The problem of conjugated conductive-convective heat transfer was formulated in dimensionless variables "vorticity/stream function/temperature" and solved by finite difference method. The effect of the heat flux density supplied to the bottom cover of the thermosyphon from a transformer tank on the temperature drop in the steam channel was shown based on the analysis of numerical simulation results (temperature fields and velocities of steam). The parameters of energy-saturated equipment of thermal stations were found to be controlled by an intensification of heat removal from the top cover surface of the thermosyphon
Numerical analyses of the effect of a biphasic thermosyphon vapor channel sizes on the heat transfer intensity when heat removing from a power transformer of combined heat and power station
Numerical analyses of the effect of a biphasic thermosyphon vapor channel sizes on the heat transfer intensity was conducted when heat removing from an oil tank of a power transformer of combined heat and power station (CHP). The power transformer cooling system by the closed biphasic thermosyphon was proposed. The mathematical modeling of heat transfer and phase transitions of coolant in the thermosyphon was performed. The problem of heat transfer is formulated in dimensionless variables "velocity vorticity vector - current function - temperature" and solved by finite difference method. As a result of numerical simulation it is found that an increase in the vapor channel length from 0.15m to 1m leads to increasing the temperature difference by 3.5 K
Peculiarities of temperature fields formation in vapor channels of thermosyphons with heat carriers boiling at low temperatures
We conducted experiments on specially developed setup consisting of evaporation, transport and condensation parts. Heat was supplied to the evaporation part by the heating element which was supplied with voltage and alternating current from a single-phase transformer. Temperatures in the characteristic sections of each part were recorded by thermocouples. Junctions of thermocouples were mounted on the axis of symmetry in the liquid layer, at the lower boundary, in the middle part, and at the upper boundary of the vapor channel. To minimize the influence of the random factors (ambient air movement, operation of ventilation system, room temperature, etc.), we placed thermosyphon in a glass box. We used N-pentane as a heat carrier, and the filling ratio of the thermosyphon is equal to 4%
Critical heat flux density in diphasic thermosyphons
The paper presents an analysis of known dependencies for determining the critical heat flux density in diphasic thermosyphons. The critical heat flux density for the created experimental model of thermosyphon were calculated on the basis of the theoretical contributions of 1) the occurrence of a βfloodingβ regime in a thermosyphon characterized by a disturbance of the hydrodynamic stability of the phase interface and the entrainment of the liquid phase by the gas flow; 2) the mutual influence of gravitational forces and surface tension; 3) S.S. Kutateladze hydrodynamic theory of the heat transfer crisis during boiling. It is found that the existing theoretical contributions which can be used to calculate the critical heat flux density and subsequently determine the minimum filling ratio of a thermosyphon are conditionally applicable
Experimental Research of Thermophysical Processes in A Closed Two-Phase Thermosyphon
The temperature distribution in a thermosyphon was studied experimentally. To conduct the research, a closed two-phase thermosyphon was developed, which differs from the known by simple construction. The method of studying the rapid processes of conduction, convection and phase transitions was also developed. It will allow to highlight the operational modes of the thermosyphon, considering the load, cooling conditions of the condensation section, value of the heat supply. According to obtained results the instabilities of the temperature fields over the cross-section of the two-phase closed thermosyphon were observed by means of using the modern measuring equipment. It has been suggested that the instabilities can be caused by different modes of thermosyphon operation
An experimental study of the influence of a thermosyphon filling ratio on a temperature distribution in characteristic points along the vapor channel height
Results of experimental studies of heat transfer in a thermosyphon illustrating the influence of the filling ratio and the heat load on the temperature distribution in the vapor channel, evaporation and condensation zones are presented. The thermosyphon was made of copper and was 161 mm high with side walls 1.5 mm thick, bottom cover 2 mm thick, an internal dimmer of the evaporation part of 54 mm and an internal diameter of the vapor channel of 39.2 mm. Based on the results of experimental studies, temperature dependences were established in the characteristic cross sections of the thermosyphon on the heat flux value supplied to the bottom cover. In addition, a well-appearing thermosyphon self-regulation property has been found β the growth of the heat load in the evaporation zone in the range from 1940 to 7685 W/m{2} does not lead to a decrease in the heat removal intensity from the heat-release region
Critical heat flux density in diphasic thermosyphons
The paper presents an analysis of known dependencies for determining the critical heat flux density in diphasic thermosyphons. The critical heat flux density for the created experimental model of thermosyphon were calculated on the basis of the theoretical contributions of 1) the occurrence of a βfloodingβ regime in a thermosyphon characterized by a disturbance of the hydrodynamic stability of the phase interface and the entrainment of the liquid phase by the gas flow; 2) the mutual influence of gravitational forces and surface tension; 3) S.S. Kutateladze hydrodynamic theory of the heat transfer crisis during boiling. It is found that the existing theoretical contributions which can be used to calculate the critical heat flux density and subsequently determine the minimum filling ratio of a thermosyphon are conditionally applicable
Experimental study of temperatures in characteristic sections of the working zone of a closed two-phase thermosyphon under the condition of a heat removal by external periphery
We present the results of the experimental study of temperature fields in a closed two-phase thermosyphon. Operational modes of a thermosyphon with different heat supply conditions are studied experimentally using setup consisting of the copper case, systems of heat supply and removal in evaporation and condensation zones, and temperature recording facilities. The height of the heat exchanger is 161 mm, thickness of the side walls and bottom wall are 1.5 mm and 2 mm, respectively, inner diameter is 39 mm. Heat is supplied to the bottom wall by heating element. The heat carrier is distilled water. We obtained thermograms when heat fluxes to the bottom wall of the thermosyphon are 695 - 2136 W/m{2}
Analysis of potential method of geothermal energy application
ΠΡΠΎΠ²Π΅Π΄Π΅Π½ΠΎ ΡΠΈΡΠ»Π΅Π½Π½ΠΎΠ΅ ΠΌΠΎΠ΄Π΅Π»ΠΈΡΠΎΠ²Π°Π½ΠΈΠ΅ ΠΏΡΠΎΡΠ΅ΡΡΠΎΠ² ΡΠ΅ΠΏΠ»ΠΎΠΏΠ΅ΡΠ΅Π½ΠΎΡΠ° Π² ΠΊΠ°ΡΠΊΠ°Π΄Π΅ ΡΠ΅ΡΠΌΠΎΡΠΈΡΠΎΠ½ΠΎΠ², ΠΏΡΠ΅Π΄ΡΡΠ°Π²Π»ΡΡΡΠΈΡ
ΡΠΎΠ±ΠΎΠΉ ΡΠΈΡΡΠ΅ΠΌΡ ΠΈΠ·Π²Π»Π΅ΡΠ΅Π½ΠΈΡ Π³Π΅ΠΎΡΠ΅ΡΠΌΠ°Π»ΡΠ½ΠΎΠΉ ΡΠ½Π΅ΡΠ³ΠΈΠΈ Ρ Π±ΠΎΠ»ΡΡΠΈΡ
Π³Π»ΡΠ±ΠΈΠ½. ΠΡΠ΅Π΄Π»ΠΎΠΆΠ΅Π½Π° ΠΌΠ°ΡΠ΅ΠΌΠ°ΡΠΈΡΠ΅ΡΠΊΠ°Ρ ΠΌΠΎΠ΄Π΅Π»Ρ ΡΠ΅ΠΏΠ»ΠΎΠΏΠ΅ΡΠ΅Π½ΠΎΡΠ° Π² ΡΠ»ΠΎΠ΅ ΡΠ΅ΠΏΠ»ΠΎΠ½ΠΎΡΠΈΡΠ΅Π»Ρ Π½Π° Π½ΠΈΠΆΠ½Π΅ΠΉ ΠΊΡΡΡΠΊΠ΅ ΡΠ΅ΡΠΌΠΎΡΠΈΡΠΎΠ½Π° ΠΈ ΠΏΠ°ΡΠΎΠ²ΠΎΠΌ ΠΊΠ°Π½Π°Π»Π΅, ΠΎΡΠ»ΠΈΡΠ°ΡΡΠΈΡ
ΡΡ ΠΎΡ ΠΈΠ·Π²Π΅ΡΡΠ½ΡΡ
ΡΠΏΡΠΎΡΠ΅Π½Π½ΡΠΌ ΠΎΠΏΠΈΡΠ°Π½ΠΈΠ΅ΠΌ ΠΊΠΎΠΌΠΏΠ»Π΅ΠΊΡΠ° ΡΠ΅ΠΏΠ»ΠΎΡΠΈΠ·ΠΈΡΠ΅ΡΠΊΠΈΡ
ΠΏΡΠΎΡΠ΅ΡΡΠΎΠ², ΠΏΡΠΎΡΠ΅ΠΊΠ°ΡΡΠΈΡ
Π² Π·ΠΎΠ½Π°Ρ
ΠΈΡΠΏΠ°ΡΠ΅Π½ΠΈΡ, ΡΡΠ°Π½ΡΠΏΠΎΡΡΠ° ΠΈ ΠΊΠΎΠ½Π΄Π΅Π½ΡΠ°ΡΠΈΠΈ ΡΠ΅ΡΠΌΠΎΡΠΈΡΠΎΠ½Π°. Π¦Π΅Π»ΡΡ ΠΈΡΡΠ»Π΅Π΄ΠΎΠ²Π°Π½ΠΈΡ ΡΠ²Π»ΡΠ΅ΡΡΡ ΡΠ°Π·ΡΠ°Π±ΠΎΡΠΊΠ° ΡΠΏΡΠΎΡΠ΅Π½Π½ΠΎΠ³ΠΎ ΠΌΠ΅ΡΠΎΠ΄Π° ΡΠ°ΡΡΠ΅ΡΠ° ΡΠ΅ΠΌΠΏΠ΅ΡΠ°ΡΡΡΠ½ΡΡ
ΠΏΠΎΠ»Π΅ΠΉ Π² ΠΊΠ°ΡΠΊΠ°Π΄Π΅ ΡΠ΅ΡΠΌΠΎΡΠΈΡΠΎΠ½ΠΎΠ², ΠΎΠ±Π΅ΡΠΏΠ΅ΡΠΈΠ²Π°ΡΡΠ΅Π³ΠΎ Π²ΠΎΠ·ΠΌΠΎΠΆΠ½ΠΎΡΡΡ ΠΏΡΠΎΠ²Π΅Π΄Π΅Π½ΠΈΡ ΠΎΠΏΡΡΠ½ΠΎ-ΠΊΠΎΠ½ΡΡΡΡΠΊΡΠΎΡΡΠΊΠΈΡ
ΡΠ°Π±ΠΎΡ ΠΏΠΎ ΡΠΎΠ·Π΄Π°Π½ΠΈΡ ΡΠΈΡΡΠ΅ΠΌ ΠΈΠ·Π²Π»Π΅ΡΠ΅Π½ΠΈΡ Π³Π΅ΠΎΡΠ΅ΡΠΌΠ°Π»ΡΠ½ΠΎΠΉ ΡΠ½Π΅ΡΠ³ΠΈΠΈ Π½Π° ΠΎΡΠ½ΠΎΠ²Π΅ ΠΊΠ°ΡΠΊΠ°Π΄Π° ΡΠ΅ΡΠΌΠΎΡΠΈΡΠΎΠ½ΠΎΠ². ΠΡΠ°Π΅Π²Π°Ρ Π·Π°Π΄Π°ΡΠ° ΠΌΠ°ΡΠ΅ΠΌΠ°ΡΠΈΡΠ΅ΡΠΊΠΎΠΉ ΡΠΈΠ·ΠΈΠΊΠΈ ΡΠ΅ΡΠ°Π»Π°ΡΡ ΠΌΠ΅ΡΠΎΠ΄ΠΎΠΌ ΠΊΠΎΠ½Π΅ΡΠ½ΡΡ
ΡΠ°Π·Π½ΠΎΡΡΠ΅ΠΉ. ΠΠΎΠΊΠ°Π·Π°Π½Π° Π²ΠΎΠ·ΠΌΠΎΠΆΠ½ΠΎΡΡΡ Π°Π½Π°Π»ΠΈΠ·Π° ΠΎΡΠ½ΠΎΠ²Π½ΡΡ
Ρ
Π°ΡΠ°ΠΊΡΠ΅ΡΠΈΡΡΠΈΠΊ β ΡΠ΅ΠΌΠΏΠ΅ΡΠ°ΡΡΡ β Π² ΡΠ°ΠΌΠΊΠ°Ρ
ΠΌΠΎΠ΄Π΅Π»ΠΈ Β«ΡΡΡΠ΅ΠΊΡΠΈΠ²Π½ΠΎΠΉΒ» ΡΠ΅ΠΏΠ»ΠΎΠΏΡΠΎΠ²ΠΎΠ΄Π½ΠΎΡΡΠΈ, ΠΊΠΎΡΡΡΠΈΡΠΈΠ΅Π½ΡΡ ΠΏΠ΅ΡΠ΅Π½ΠΎΡΠ° ΠΊΠΎΡΠΎΡΠΎΠΉ ΠΌΠΎΠ³ΡΡ Π±ΡΡΡ ΠΎΠΏΡΠ΅Π΄Π΅Π»Π΅Π½Ρ ΡΠΊΡΠΏΠ΅ΡΠΈΠΌΠ΅Π½ΡΠ°Π»ΡΠ½ΠΎ. Π£ΡΡΠ°Π½ΠΎΠ²Π»Π΅Π½Π° Π²ΠΎΠ·ΠΌΠΎΠΆΠ½ΠΎΡΡΡ ΠΏΠ΅ΡΠ΅Π½ΠΎΡΠ° ΡΠ΅ΠΏΠ»ΠΎΡΡ Ρ Π±ΠΎΠ»ΡΡΠΈΡ
Π³Π»ΡΠ±ΠΈΠ½ Ρ Β«ΡΡΡΠ΅ΠΊΡΠΈΠ²Π½ΠΎΡΡΡΡΒ», Π΄ΠΎΡΡΠ°ΡΠΎΡΠ½ΠΎΠΉ Π΄Π»Ρ Π΄ΠΎΡΡΠΈΠΆΠ΅Π½ΠΈΡ Π² ΡΠΈΡΡΠ΅ΠΌΠ΅ ΡΠ΅ΠΏΠ»ΠΎΡΠ½Π°Π±ΠΆΠ΅Π½ΠΈΡ ΡΠ΅ΠΌΠΏΠ΅ΡΠ°ΡΡΡ ΠΎΠΊΠΎΠ»ΠΎ 330 Π Π² ΡΡΠ»ΠΎΠ²ΠΈΡΡ
ΠΏΠΎΠ»Π½ΠΎΠΉ ΡΠ΅ΠΏΠ»ΠΎΠΈΠ·ΠΎΠ»ΡΡΠΈΠΈ Π²Π½Π΅ΡΠ½Π΅Π³ΠΎ ΠΊΠΎΠ½ΡΡΡΠ° (ΠΏΠΎΠ²Π΅ΡΡ
Π½ΠΎΡΡΠ΅ΠΉ ΡΠ΅ΡΠΌΠΎΡΠΈΡΠΎΠ½Π°). ΠΠΎΠ»ΡΡΠ΅Π½Π½ΡΠ΅ ΡΠ΅Π·ΡΠ»ΡΡΠ°ΡΡ ΡΠ²Π»ΡΡΡΡΡ Π±Π°Π·ΠΎΠΉ Π΄Π»Ρ Π΄Π°Π»ΡΠ½Π΅ΠΉΡΠ΅Π³ΠΎ ΡΠ°Π·Π²ΠΈΡΠΈΡ ΠΌΠΎΠ΄Π΅Π»Π΅ΠΉ ΠΈ ΠΌΠ΅ΡΠΎΠ΄ΠΎΠ² Π°Π½Π°Π»ΠΈΠ·Π° ΠΏΡΠΎΡΠ΅ΡΡΠΎΠ² ΠΈΠ·Π²Π»Π΅ΡΠ΅Π½ΠΈΡ Π³Π΅ΠΎΡΠ΅ΡΠΌΠ°Π»ΡΠ½ΠΎΠΉ ΡΠ½Π΅ΡΠ³ΠΈΠΈ Ρ Π±ΠΎΠ»ΡΡΠΈΡ
Π³Π»ΡΠ±ΠΈΠ½ Ρ ΠΈΡΠΏΠΎΠ»ΡΠ·ΠΎΠ²Π°Π½ΠΈΠ΅ΠΌ ΠΊΠ°ΡΠΊΠ°Π΄Π° ΠΏΠΎΡΠ»Π΅Π΄ΠΎΠ²Π°ΡΠ΅Π»ΡΠ½ΠΎ ΡΠ°Π±ΠΎΡΠ°ΡΡΠΈΡ
ΡΠ΅ΡΠΌΠΎΡΠΈΡΠΎΠ½ΠΎΠ². ΠΠΎ ΡΠ΅Π·ΡΠ»ΡΡΠ°ΡΠ°ΠΌ ΠΏΠΎΠ»ΡΡΠ΅Π½Π½ΡΡ
ΡΠ΅ΠΎΡΠ΅ΡΠΈΡΠ΅ΡΠΊΠΈΡ
ΡΠ»Π΅Π΄ΡΡΠ²ΠΈΠΉ ΡΡΠΎΡΠΌΡΠ»ΠΈΡΠΎΠ²Π°Π½Ρ ΠΎΡΠ½ΠΎΠ²Π½ΡΠ΅ Π½Π°ΠΏΡΠ°Π²Π»Π΅Π½ΠΈΡ ΡΠΊΡΠΏΠ΅ΡΠΈΠΌΠ΅Π½ΡΠ°Π»ΡΠ½ΡΡ
ΠΈΡΡΠ»Π΅Π΄ΠΎΠ²Π°Π½ΠΈΠΉ Ρ ΡΠ΅Π»ΡΡ ΠΎΠ±ΠΎΡΠ½ΠΎΠ²Π°Π½ΠΈΡ ΡΠ΄Π΅Π»Π°Π½Π½ΡΡ
ΠΏΠΎ ΡΠ΅Π·ΡΠ»ΡΡΠ°ΡΠ°ΠΌ ΡΠΈΡΠ»Π΅Π½Π½ΠΎΠ³ΠΎ Π°Π½Π°Π»ΠΈΠ·Π° Π²ΡΠ²ΠΎΠ΄ΠΎΠ². Π Π΅Π·ΡΠ»ΡΡΠ°ΡΡ ΡΠΈΡΠ»Π΅Π½Π½ΠΎΠ³ΠΎ ΠΌΠΎΠ΄Π΅Π»ΠΈΡΠΎΠ²Π°Π½ΠΈΡ Π΄Π°ΡΡ ΠΎΡΠ½ΠΎΠ²Π°Π½ΠΈΡ Π΄Π»Ρ Π²ΡΠ²ΠΎΠ΄Π° ΠΎ ΠΏΠ΅ΡΡΠΏΠ΅ΠΊΡΠΈΠ²Π½ΠΎΡΡΠΈ Π΄Π°Π»ΡΠ½Π΅ΠΉΡΠ΅ΠΉ (ΡΠΊΡΠΏΠ΅ΡΠΈΠΌΠ΅Π½ΡΠ°Π»ΡΠ½ΠΎΠΉ ΠΈ ΡΠ΅ΠΎΡΠ΅ΡΠΈΡΠ΅ΡΠΊΠΎΠΉ) ΡΠ°Π·ΡΠ°Π±ΠΎΡΠΊΠΈ ΠΌΠ΅ΡΠΎΠ΄Π° ΠΈΠ·Π²Π»Π΅ΡΠ΅Π½ΠΈΡ Π³Π΅ΠΎΡΠ΅ΡΠΌΠ°Π»ΡΠ½ΠΎΠΉ ΡΠ½Π΅ΡΠ³ΠΈΠΈ Ρ Π±ΠΎΠ»ΡΡΠΈΡ
Π³Π»ΡΠ±ΠΈΠ½ Π·Π°Π»Π΅Π³Π°Π½ΠΈΡ Π³ΡΡΠ½ΡΠΎΠ²ΡΡ
Π²ΠΎΠ΄ Ρ ΠΈΡΠΏΠΎΠ»ΡΠ·ΠΎΠ²Π°Π½ΠΈΠ΅ΠΌ ΠΊΠ°ΡΠΊΠ°Π΄Π° ΡΠ΅ΡΠΌΠΎΡΠΈΡΠΎΠ½ΠΎΠ² Π±ΠΎΠ»ΡΡΠΎΠΉ Π²ΡΡΠΎΡΡ.The numerical simulation of heat transfer was conducted in a cascade of thermosyphons representing a system for extracting geother- mal energy from great depths. We proposed a mathematical model of heat transfer in the coolant layer on the bottom cover of a ther- mosyphon and in the vapor channel differing from the well- plified method for calculating temperature fields in a cascade of thermosyphons, which makes it possible to conduct design and expe- rimental work to create the systems for extracting geothermal energy based on a cascade of thermosyphons. The boundary problem of mathematical physics was solved by the method of finite differences. We showed the possibility to analyze the main characteristics - temperatures - within the framework of the model of Β«effectiveΒ» thermal conductivity. The transfer coefficients of this model can be determined experimentally. We found the possibility of heat transfer from large depths with Β«efficiencyΒ» sufficient to achieve tempe- ratures of about 330 K in the heat supply system when the external contour (thermosyphon surfaces) is completely thermally insulated. The results obtained are the basis for the further development of models and methods for analyzing geothermal energy extraction from great depths using a cascade of sequentially operating thermosyphons. According to the obtained theoretical results, the main directions of experimental studies were formulated to justify the conclusions made by the results of a numerical analysis. The results of numerical simulation provide grounds for concluding that the future (experimental and theoretical) development of a method for extracting geothermal energy from large depths of groundwater using a cascade of thermosyphons is promising