Abstract:SUMMARY
In this study, the heat transfer performance and friction characteristics of a novel concentric tube heat exchanger with different pitches of helical turbulators were investigated experimentally and numerically for a Reynolds number range from 3000 to 14 000. An experimental system was established to obtain experimental data. The numerical simulations were performed by using a three dimensional numerical computation technique, a commercial CFD computer code. Then, the heat transfer performance and fric… Show more
“…The uncertainties of experimental results for m · , Q · , h, Nu, Re, D P and f were estimated to be ±4.3%, ±4.3%, ±4.4%, ±4.7%, ±4.7%, ±5.9% and ±6.7%, respectively. In the same conditions, the experimental results can be reproduced for these uncertainty ranges in this study [12].…”
Section: Experimental Uncertaintymentioning
confidence: 65%
“…The hot air and cold water enter in the opposite ends of the heat exchanger and flow in opposite directions. The hot air flows in the inner tube, while the cold water flows in the outer tube [12]. The diameters of the inner tube (D) and outer tube are 40 mm and 69 mm, respectively.…”
Section: Methodsmentioning
confidence: 99%
“…1 shows the schematic diagram of the experimental setup connected to the data logger and analysis system, positions of the thermocouples, other measurement instruments, a concentric tube heat exchanger and used tools [12]. The inlet bulk air at 22 C from the laboratory room was directed through a 0.6 kW blower adjusted flow rates by changeable motor speed via the inverter (ABB ACS350 model) located at the system.…”
Section: Methodsmentioning
confidence: 99%
“…where, r is density, u velocity, m dynamic viscosity, p pressure, k thermal conductivity, T temperature and cp specific heat [12].…”
Section: Numerical Calculationmentioning
confidence: 99%
“…Moreover, there were not any convergence problems. Thus, this uniform grid was used for all range of Re number to solve each equation of the continuity, momentum and turbulent [12].…”
“…The uncertainties of experimental results for m · , Q · , h, Nu, Re, D P and f were estimated to be ±4.3%, ±4.3%, ±4.4%, ±4.7%, ±4.7%, ±5.9% and ±6.7%, respectively. In the same conditions, the experimental results can be reproduced for these uncertainty ranges in this study [12].…”
Section: Experimental Uncertaintymentioning
confidence: 65%
“…The hot air and cold water enter in the opposite ends of the heat exchanger and flow in opposite directions. The hot air flows in the inner tube, while the cold water flows in the outer tube [12]. The diameters of the inner tube (D) and outer tube are 40 mm and 69 mm, respectively.…”
Section: Methodsmentioning
confidence: 99%
“…1 shows the schematic diagram of the experimental setup connected to the data logger and analysis system, positions of the thermocouples, other measurement instruments, a concentric tube heat exchanger and used tools [12]. The inlet bulk air at 22 C from the laboratory room was directed through a 0.6 kW blower adjusted flow rates by changeable motor speed via the inverter (ABB ACS350 model) located at the system.…”
Section: Methodsmentioning
confidence: 99%
“…where, r is density, u velocity, m dynamic viscosity, p pressure, k thermal conductivity, T temperature and cp specific heat [12].…”
Section: Numerical Calculationmentioning
confidence: 99%
“…Moreover, there were not any convergence problems. Thus, this uniform grid was used for all range of Re number to solve each equation of the continuity, momentum and turbulent [12].…”
The heat transfer and pressure drop characteristics in annuli of a double-pipe heat exchanger (DPHE) using helical surface disc turbulators (HSDTs) are experimentally investigated. The effect of a helical surface disc turbulator is studied for three pitch ratios, three diameter ratios, and varying Reynolds numbers. Water flows in the inner tube and air through the annulus. The tests are conducted for air with uniform wall temperature condition. The heat exchanger with the least pitch ratio and least diameter ratio was found to exhibit the highest Nusselt number and pressure drop. The thermal performance factor turned out to be greater than unity for all cases. Correlations were developed for Nusselt number, friction factor, and thermal performance.
SUMMARYIntegrated pressurized water reactor (IPWR) usually be equipped with once-through steam generators (OTSGs). The OTSG has many advantages such as simple mechanical structure, smaller size, and higher heat transfer efficiency. It produces superheated steam but with less inventory in its secondary side. The steam pressure is easily affected by steam flow rate or feed water flow rate. This draws more attention to design advanced reactor control system. In this paper, a study has been carried out to analyze the thermal hydraulic performance of an advanced IPWR under steady-state and transient conditions by using a thermal hydraulic safety analysis code Relap5. An effective load-following control system is proposed. The steady-state operating characteristics of IPWR at different load conditions show that the average primary coolant temperature, steam pressure, and coolant mass flow rate are the most important control parameters. Pump frequency conversion strategy and OTSG grouping run strategy are used to study the transient operating characteristics of IPWR. Simulation results of the control system demonstrate its capability in regulating feedwater flow rate and reactor power to follow the change of steam flow rate. According to the results, the OTSG grouping run strategy is optimized to ensure the OTSG operates safely under low load conditions.
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