11 research outputs found

    Mathematical modeling heat transfer in closed two-phase thermosyphon

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    ΠŸΡ€ΠΎΠ²Π΅Π΄Π΅Π½ числСнный Π°Π½Π°Π»ΠΈΠ· тСплопСрСноса Π² Π·Π°ΠΌΠΊΠ½ΡƒΡ‚ΠΎΠΌ Π΄Π²ΡƒΡ…Ρ„Π°Π·Π½ΠΎΠΌ тСрмосифонС цилиндричСской Ρ„ΠΎΡ€ΠΌΡ‹ Π² условии ΠΏΠΎΠ΄Π²ΠΎΠ΄Π° Ρ‚Π΅ΠΏΠ»ΠΎΡ‚Ρ‹ Π½Π° Π½ΠΈΠΆΠ½Π΅ΠΉ ΠΊΡ€Ρ‹ΡˆΠΊΠ΅. Для описания исслСдуСмого процСсса ΠΏΡ€Π΅Π΄Π»ΠΎΠΆΠ΅Π½Π° упрощСнная матСматичСская модСль, ΠΎΡ‚Π»ΠΈΡ‡Π°ΡŽΡ‰Π°ΡΡΡ ΠΎΡ‚ извСстной описаниСм Ρ‚ΠΎΠ»ΡŒΠΊΠΎ процСссов тСплопроводности Π² систСмС "корпус тСрмосифона - ΠΏΠ°Ρ€ΠΎΠ²ΠΎΠΉ ΠΊΠ°Π½Π°Π» - ΠΏΠ»Π΅Π½ΠΊΠ° кондСнсата". Бформулированная краСвая Π·Π°Π΄Π°Ρ‡Π° Ρ€Π΅ΡˆΠ΅Π½Π° ΠΌΠ΅Ρ‚ΠΎΠ΄ΠΎΠΌ ΠΊΠΎΠ½Π΅Ρ‡Π½Ρ‹Ρ… разностСй. ΠŸΠΎΠ»ΡƒΡ‡Π΅Π½Ρ‹ поля Ρ‚Π΅ΠΌΠΏΠ΅Ρ€Π°Ρ‚ΡƒΡ€ Π² тСрмосифонС для Ρ‚ΠΈΠΏΠΈΡ‡Π½Ρ‹Ρ… Ρ‚Π΅ΠΏΠ»ΠΎΠ²Ρ‹Ρ… Π½Π°Π³Ρ€ΡƒΠ·ΠΎΠΊ ΠΈ Ρ€Π΅ΠΆΠΈΠΌΠΎΠ² Ρ€Π°Π±ΠΎΡ‚Ρ‹

    The Opportunity Analyses of Using Thermosyphons in Cooling Systems of Power Transformers on Thermal Stations

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    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

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    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

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    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

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    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 β€œflooding” 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

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    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

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    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 – 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

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    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 β€œflooding” 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

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    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

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    ΠŸΡ€ΠΎΠ²Π΅Π΄Π΅Π½ΠΎ числСнноС ΠΌΠΎΠ΄Π΅Π»ΠΈΡ€ΠΎΠ²Π°Π½ΠΈΠ΅ процСссов тСплопСрСноса Π² каскадС тСрмосифонов, ΠΏΡ€Π΅Π΄ΡΡ‚Π°Π²Π»ΡΡŽΡ‰ΠΈΡ… собой систСму извлСчСния Π³Π΅ΠΎΡ‚Π΅Ρ€ΠΌΠ°Π»ΡŒΠ½ΠΎΠΉ энСргии с Π±ΠΎΠ»ΡŒΡˆΠΈΡ… Π³Π»ΡƒΠ±ΠΈΠ½. ΠŸΡ€Π΅Π΄Π»ΠΎΠΆΠ΅Π½Π° матСматичСская модСль тСплопСрСноса Π² слоС тСплоноситСля Π½Π° Π½ΠΈΠΆΠ½Π΅ΠΉ ΠΊΡ€Ρ‹ΡˆΠΊΠ΅ тСрмосифона ΠΈ ΠΏΠ°Ρ€ΠΎΠ²ΠΎΠΌ ΠΊΠ°Π½Π°Π»Π΅, ΠΎΡ‚Π»ΠΈΡ‡Π°ΡŽΡ‰ΠΈΡ…ΡΡ ΠΎΡ‚ извСстных ΡƒΠΏΡ€ΠΎΡ‰Π΅Π½Π½Ρ‹ΠΌ описаниСм комплСкса тСплофизичСских процСссов, ΠΏΡ€ΠΎΡ‚Π΅ΠΊΠ°ΡŽΡ‰ΠΈΡ… Π² Π·ΠΎΠ½Π°Ρ… испарСния, транспорта ΠΈ кондСнсации тСрмосифона. ЦСлью исслСдования являСтся Ρ€Π°Π·Ρ€Π°Π±ΠΎΡ‚ΠΊΠ° ΡƒΠΏΡ€ΠΎΡ‰Π΅Π½Π½ΠΎΠ³ΠΎ ΠΌΠ΅Ρ‚ΠΎΠ΄Π° расчСта Ρ‚Π΅ΠΌΠΏΠ΅Ρ€Π°Ρ‚ΡƒΡ€Π½Ρ‹Ρ… ΠΏΠΎΠ»Π΅ΠΉ Π² каскадС тСрмосифонов, ΠΎΠ±Π΅ΡΠΏΠ΅Ρ‡ΠΈΠ²Π°ΡŽΡ‰Π΅Π³ΠΎ Π²ΠΎΠ·ΠΌΠΎΠΆΠ½ΠΎΡΡ‚ΡŒ провСдСния ΠΎΠΏΡ‹Ρ‚Π½ΠΎ-конструкторских Ρ€Π°Π±ΠΎΡ‚ ΠΏΠΎ созданию систСм извлСчСния Π³Π΅ΠΎΡ‚Π΅Ρ€ΠΌΠ°Π»ΡŒΠ½ΠΎΠΉ энСргии Π½Π° основС каскада тСрмосифонов. ΠšΡ€Π°Π΅Π²Π°Ρ Π·Π°Π΄Π°Ρ‡Π° матСматичСской Ρ„ΠΈΠ·ΠΈΠΊΠΈ Ρ€Π΅ΡˆΠ°Π»Π°ΡΡŒ ΠΌΠ΅Ρ‚ΠΎΠ΄ΠΎΠΌ ΠΊΠΎΠ½Π΅Ρ‡Π½Ρ‹Ρ… разностСй. Показана Π²ΠΎΠ·ΠΌΠΎΠΆΠ½ΠΎΡΡ‚ΡŒ Π°Π½Π°Π»ΠΈΠ·Π° основных характСристик – Ρ‚Π΅ΠΌΠΏΠ΅Ρ€Π°Ρ‚ΡƒΡ€ – Π² Ρ€Π°ΠΌΠΊΠ°Ρ… ΠΌΠΎΠ΄Π΅Π»ΠΈ «эффСктивной» тСплопроводности, коэффициСнты пСрСноса ΠΊΠΎΡ‚ΠΎΡ€ΠΎΠΉ ΠΌΠΎΠ³ΡƒΡ‚ Π±Ρ‹Ρ‚ΡŒ ΠΎΠΏΡ€Π΅Π΄Π΅Π»Π΅Π½Ρ‹ ΡΠΊΡΠΏΠ΅Ρ€ΠΈΠΌΠ΅Π½Ρ‚Π°Π»ΡŒΠ½ΠΎ. УстановлСна Π²ΠΎΠ·ΠΌΠΎΠΆΠ½ΠΎΡΡ‚ΡŒ пСрСноса Ρ‚Π΅ΠΏΠ»ΠΎΡ‚Ρ‹ с Π±ΠΎΠ»ΡŒΡˆΠΈΡ… Π³Π»ΡƒΠ±ΠΈΠ½ с Β«ΡΡ„Ρ„Π΅ΠΊΡ‚ΠΈΠ²Π½ΠΎΡΡ‚ΡŒΡŽΒ», достаточной для достиТСния Π² систСмС тСплоснабТСния Ρ‚Π΅ΠΌΠΏΠ΅Ρ€Π°Ρ‚ΡƒΡ€ ΠΎΠΊΠΎΠ»ΠΎ 330 К Π² условиях ΠΏΠΎΠ»Π½ΠΎΠΉ тСплоизоляции внСшнСго ΠΊΠΎΠ½Ρ‚ΡƒΡ€Π° (повСрхностСй тСрмосифона). ΠŸΠΎΠ»ΡƒΡ‡Π΅Π½Π½Ρ‹Π΅ Ρ€Π΅Π·ΡƒΠ»ΡŒΡ‚Π°Ρ‚Ρ‹ ΡΠ²Π»ΡΡŽΡ‚ΡΡ Π±Π°Π·ΠΎΠΉ для дальнСйшСго развития ΠΌΠΎΠ΄Π΅Π»Π΅ΠΉ ΠΈ ΠΌΠ΅Ρ‚ΠΎΠ΄ΠΎΠ² Π°Π½Π°Π»ΠΈΠ·Π° процСссов извлСчСния Π³Π΅ΠΎΡ‚Π΅Ρ€ΠΌΠ°Π»ΡŒΠ½ΠΎΠΉ энСргии с Π±ΠΎΠ»ΡŒΡˆΠΈΡ… Π³Π»ΡƒΠ±ΠΈΠ½ с использованиСм каскада ΠΏΠΎΡΠ»Π΅Π΄ΠΎΠ²Π°Ρ‚Π΅Π»ΡŒΠ½ΠΎ Ρ€Π°Π±ΠΎΡ‚Π°ΡŽΡ‰ΠΈΡ… тСрмосифонов. По Ρ€Π΅Π·ΡƒΠ»ΡŒΡ‚Π°Ρ‚Π°ΠΌ ΠΏΠΎΠ»ΡƒΡ‡Π΅Π½Π½Ρ‹Ρ… тСорСтичСских слСдствий сформулированы основныС направлСния ΡΠΊΡΠΏΠ΅Ρ€ΠΈΠΌΠ΅Π½Ρ‚Π°Π»ΡŒΠ½Ρ‹Ρ… исслСдований с Ρ†Π΅Π»ΡŒΡŽ обоснования сдСланных ΠΏΠΎ Ρ€Π΅Π·ΡƒΠ»ΡŒΡ‚Π°Ρ‚Π°ΠΌ числСнного Π°Π½Π°Π»ΠΈΠ·Π° Π²Ρ‹Π²ΠΎΠ΄ΠΎΠ². Π Π΅Π·ΡƒΠ»ΡŒΡ‚Π°Ρ‚Ρ‹ числСнного модСлирования Π΄Π°ΡŽΡ‚ основания для Π²Ρ‹Π²ΠΎΠ΄Π° ΠΎ пСрспСктивности дальнСйшСй (ΡΠΊΡΠΏΠ΅Ρ€ΠΈΠΌΠ΅Π½Ρ‚Π°Π»ΡŒΠ½ΠΎΠΉ ΠΈ тСорСтичСской) Ρ€Π°Π·Ρ€Π°Π±ΠΎΡ‚ΠΊΠΈ ΠΌΠ΅Ρ‚ΠΎΠ΄Π° извлСчСния Π³Π΅ΠΎΡ‚Π΅Ρ€ΠΌΠ°Π»ΡŒΠ½ΠΎΠΉ энСргии с Π±ΠΎΠ»ΡŒΡˆΠΈΡ… Π³Π»ΡƒΠ±ΠΈΠ½ залСгания Π³Ρ€ΡƒΠ½Ρ‚ΠΎΠ²Ρ‹Ρ… Π²ΠΎΠ΄ с использованиСм каскада тСрмосифонов большой высоты.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
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