SOONTORNCHAINACKSAENG, Thanakom . Experimentation and Simulation of Thermal Energy Storage System with Non-Phase Change Materials. Strojniški vestnik - Journal of Mechanical Engineering, [S.l.], v. 51, n.7-8, p. 534-537, august 2017. ISSN 0039-2480. Available at: <https://www.sv-jme.eu/article/experimentation-and-simulation-of-thermal-energy-storage-system-with-non-phase-change-materials/>. Date accessed: 20 dec. 2024. doi:http://dx.doi.org/.
Soontornchainacksaeng, T. (2005). Experimentation and Simulation of Thermal Energy Storage System with Non-Phase Change Materials. Strojniški vestnik - Journal of Mechanical Engineering, 51(7-8), 534-537. doi:http://dx.doi.org/
@article{.,
author = {Thanakom Soontornchainacksaeng},
title = {Experimentation and Simulation of Thermal Energy Storage System with Non-Phase Change Materials},
journal = {Strojniški vestnik - Journal of Mechanical Engineering},
volume = {51},
number = {7-8},
year = {2005},
keywords = {Thermal Energy; Non-Phase Change Materials; },
abstract = {This research a simulation study and experiment on the thermal energy storage system with non-phase change materials in the range of 50q - 150qC, this system is consisted of the storage tank size of 0.58 m in diameter, and 0.88 m in height, containing each set of the charging coil, and the discharging coil, embedded in the combination of 90% by volume of the used – engine oil, and 10% by volume of the river – water rocks. An electric heater is used as the heat source. The simulation of thermal-energy storage system with the mathematic modeling for the theoretical analysis of the system, and by using the Newton – Raphson method in the simulation process during the energy charging and discharging processes, The limitation of the charging oil temperature is maintained at 140qC with the flow rate in the range of 10 to18 l/min, whereas the inlet temperature of the discharge oil is maintained at 30qC with the flow rate of 6 to 14 l/min. The computer simulation results with the charging time of 2 hours, and the oil flow rate of 14 l/min, The temperature of our storage media is increased by 60qC with the amount of heat gain by 23 MJ. And by our further simulation on discharging for 1 hour period, with the oil flow rate of 10 l/min, the storage temperature is decreased by 58qC, with the amount of heat removal of 23 MJ. It is found that results from the experiment are differed from the simulation by 3–5 %},
issn = {0039-2480}, pages = {534-537}, doi = {},
url = {https://www.sv-jme.eu/article/experimentation-and-simulation-of-thermal-energy-storage-system-with-non-phase-change-materials/}
}
Soontornchainacksaeng, T. 2005 August 51. Experimentation and Simulation of Thermal Energy Storage System with Non-Phase Change Materials. Strojniški vestnik - Journal of Mechanical Engineering. [Online] 51:7-8
%A Soontornchainacksaeng, Thanakom %D 2005 %T Experimentation and Simulation of Thermal Energy Storage System with Non-Phase Change Materials %B 2005 %9 Thermal Energy; Non-Phase Change Materials; %! Experimentation and Simulation of Thermal Energy Storage System with Non-Phase Change Materials %K Thermal Energy; Non-Phase Change Materials; %X This research a simulation study and experiment on the thermal energy storage system with non-phase change materials in the range of 50q - 150qC, this system is consisted of the storage tank size of 0.58 m in diameter, and 0.88 m in height, containing each set of the charging coil, and the discharging coil, embedded in the combination of 90% by volume of the used – engine oil, and 10% by volume of the river – water rocks. An electric heater is used as the heat source. The simulation of thermal-energy storage system with the mathematic modeling for the theoretical analysis of the system, and by using the Newton – Raphson method in the simulation process during the energy charging and discharging processes, The limitation of the charging oil temperature is maintained at 140qC with the flow rate in the range of 10 to18 l/min, whereas the inlet temperature of the discharge oil is maintained at 30qC with the flow rate of 6 to 14 l/min. The computer simulation results with the charging time of 2 hours, and the oil flow rate of 14 l/min, The temperature of our storage media is increased by 60qC with the amount of heat gain by 23 MJ. And by our further simulation on discharging for 1 hour period, with the oil flow rate of 10 l/min, the storage temperature is decreased by 58qC, with the amount of heat removal of 23 MJ. It is found that results from the experiment are differed from the simulation by 3–5 % %U https://www.sv-jme.eu/article/experimentation-and-simulation-of-thermal-energy-storage-system-with-non-phase-change-materials/ %0 Journal Article %R %& 534 %P 4 %J Strojniški vestnik - Journal of Mechanical Engineering %V 51 %N 7-8 %@ 0039-2480 %8 2017-08-18 %7 2017-08-18
Soontornchainacksaeng, Thanakom. "Experimentation and Simulation of Thermal Energy Storage System with Non-Phase Change Materials." Strojniški vestnik - Journal of Mechanical Engineering [Online], 51.7-8 (2005): 534-537. Web. 20 Dec. 2024
TY - JOUR AU - Soontornchainacksaeng, Thanakom PY - 2005 TI - Experimentation and Simulation of Thermal Energy Storage System with Non-Phase Change Materials JF - Strojniški vestnik - Journal of Mechanical Engineering DO - KW - Thermal Energy; Non-Phase Change Materials; N2 - This research a simulation study and experiment on the thermal energy storage system with non-phase change materials in the range of 50q - 150qC, this system is consisted of the storage tank size of 0.58 m in diameter, and 0.88 m in height, containing each set of the charging coil, and the discharging coil, embedded in the combination of 90% by volume of the used – engine oil, and 10% by volume of the river – water rocks. An electric heater is used as the heat source. The simulation of thermal-energy storage system with the mathematic modeling for the theoretical analysis of the system, and by using the Newton – Raphson method in the simulation process during the energy charging and discharging processes, The limitation of the charging oil temperature is maintained at 140qC with the flow rate in the range of 10 to18 l/min, whereas the inlet temperature of the discharge oil is maintained at 30qC with the flow rate of 6 to 14 l/min. The computer simulation results with the charging time of 2 hours, and the oil flow rate of 14 l/min, The temperature of our storage media is increased by 60qC with the amount of heat gain by 23 MJ. And by our further simulation on discharging for 1 hour period, with the oil flow rate of 10 l/min, the storage temperature is decreased by 58qC, with the amount of heat removal of 23 MJ. It is found that results from the experiment are differed from the simulation by 3–5 % UR - https://www.sv-jme.eu/article/experimentation-and-simulation-of-thermal-energy-storage-system-with-non-phase-change-materials/
@article{{}{.},
author = {Soontornchainacksaeng, T.},
title = {Experimentation and Simulation of Thermal Energy Storage System with Non-Phase Change Materials},
journal = {Strojniški vestnik - Journal of Mechanical Engineering},
volume = {51},
number = {7-8},
year = {2005},
doi = {},
url = {https://www.sv-jme.eu/article/experimentation-and-simulation-of-thermal-energy-storage-system-with-non-phase-change-materials/}
}
TY - JOUR AU - Soontornchainacksaeng, Thanakom PY - 2017/08/18 TI - Experimentation and Simulation of Thermal Energy Storage System with Non-Phase Change Materials JF - Strojniški vestnik - Journal of Mechanical Engineering; Vol 51, No 7-8 (2005): Strojniški vestnik - Journal of Mechanical Engineering DO - KW - Thermal Energy, Non-Phase Change Materials, N2 - This research a simulation study and experiment on the thermal energy storage system with non-phase change materials in the range of 50q - 150qC, this system is consisted of the storage tank size of 0.58 m in diameter, and 0.88 m in height, containing each set of the charging coil, and the discharging coil, embedded in the combination of 90% by volume of the used – engine oil, and 10% by volume of the river – water rocks. An electric heater is used as the heat source. The simulation of thermal-energy storage system with the mathematic modeling for the theoretical analysis of the system, and by using the Newton – Raphson method in the simulation process during the energy charging and discharging processes, The limitation of the charging oil temperature is maintained at 140qC with the flow rate in the range of 10 to18 l/min, whereas the inlet temperature of the discharge oil is maintained at 30qC with the flow rate of 6 to 14 l/min. The computer simulation results with the charging time of 2 hours, and the oil flow rate of 14 l/min, The temperature of our storage media is increased by 60qC with the amount of heat gain by 23 MJ. And by our further simulation on discharging for 1 hour period, with the oil flow rate of 10 l/min, the storage temperature is decreased by 58qC, with the amount of heat removal of 23 MJ. It is found that results from the experiment are differed from the simulation by 3–5 % UR - https://www.sv-jme.eu/article/experimentation-and-simulation-of-thermal-energy-storage-system-with-non-phase-change-materials/
Soontornchainacksaeng, Thanakom"Experimentation and Simulation of Thermal Energy Storage System with Non-Phase Change Materials" Strojniški vestnik - Journal of Mechanical Engineering [Online], Volume 51 Number 7-8 (18 August 2017)
Strojniški vestnik - Journal of Mechanical Engineering 51(2005)7-8, 534-537
© The Authors, CC-BY 4.0 Int. Change in copyright policy from 2022, Jan 1st.
This research a simulation study and experiment on the thermal energy storage system with non-phase change materials in the range of 50q - 150qC, this system is consisted of the storage tank size of 0.58 m in diameter, and 0.88 m in height, containing each set of the charging coil, and the discharging coil, embedded in the combination of 90% by volume of the used – engine oil, and 10% by volume of the river – water rocks. An electric heater is used as the heat source. The simulation of thermal-energy storage system with the mathematic modeling for the theoretical analysis of the system, and by using the Newton – Raphson method in the simulation process during the energy charging and discharging processes, The limitation of the charging oil temperature is maintained at 140qC with the flow rate in the range of 10 to18 l/min, whereas the inlet temperature of the discharge oil is maintained at 30qC with the flow rate of 6 to 14 l/min. The computer simulation results with the charging time of 2 hours, and the oil flow rate of 14 l/min, The temperature of our storage media is increased by 60qC with the amount of heat gain by 23 MJ. And by our further simulation on discharging for 1 hour period, with the oil flow rate of 10 l/min, the storage temperature is decreased by 58qC, with the amount of heat removal of 23 MJ. It is found that results from the experiment are differed from the simulation by 3–5 %