Ator section; (c) the heat pipe. (a) Total heat pipe; (bAtor section; (c) the heat

Ator section; (c) the heat pipe. (a) Total heat pipe; (b
Ator section; (c) the heat pipe. (a) Total heat pipe; (b) evaporator section; Figure 32. Temperature (c) condenser section; (d) isothermal section. condenser section; (d) isothermal section.Energies 2021, 14, 7647 PEER Critique Energies 2021, 14, x FOR32 of 38 34 of(a) Fluid velocity in Figure 33. (a) Fluid velocity in the total heat pipe and within the condenser section, (b) the volume fraction of steam in the total heat pipe and within the evaporator section.14, xx FOR PEER 2-Bromo-6-nitrophenol Purity & Documentation Evaluation 14, FOR PEER REVIEWEnergies 2021, 14,35 of 40 35 of33 ofFigure 34. Temperature distribution along the height height of thepipe’s central line. Figure 34. Figure 34. Temperature distributionthe height on the heat heat pipe’s central line. Temperature distribution along along the from the heat pipe’s central line.Figure 35. Temperature distribution along the cross-section. the cross-section. Figure 35. Temperature distribution along distribution along Figure 35. Temperature the cross-section.four, x FOR PEER REVIEWEnergies 2021, 14,36 of34 ofFigure 36. Temperature distribution along the height in the heat pipe’s wall. Figure 36. Temperature distribution along the height on the heat pipe’s wall.four. Discussion4. Discussion Numerical procedures of studying Heat Pipes are usually not the subject of a lot of scientists’Numerical approaches of studying Heat Pipes are certainly not the topic of numerous scientists’ work, mostly as a result of complexity in the processes taking location inside them in the same operate, primarily duetime. In their study, the processes taking place[7] built them at the identical of a heat to the complexity of Chen as well as other co-authors inside a theoretical model time. In their study,the outcomes of which are similar[7] the results presentedmodel of a heat Around the pipe, Chen as well as other co-authors to built a theoretical in this publication. pipe, the outcomes of which areQian [8] presented a three-dimensional numerical modelOn theon comparable other hand, related for the final results presented in this publication. primarily based other hand, Qian numerical assumptions presented within this publication. In Ref. [9],on similarco-authors [8] presented a three-dimensional numerical model based Gao and focused around the structural publication. In Ref. zone of and co-authors fonumerical assumptions presented within this style in the Aztreonam Anti-infection catalytic [9], Gaothe sulfuric acid decomposition plant. design from the tube was zone with the sulfuric acid of your heat transfer cused on the structuralThe double inner catalytic created to analyze the effectsdecomposition surface of the inner tube along with the catalytic analyze the ring area on the decomposition plant. The double inner tube was created to volume ofthe effects in the heat transfer rate. The results show that the new design and style meets the decomposition temperature specifications and surface of the inner tube along with the catalytic volume of your ring area around the decomposition increases the heat flow rate, and validates the usage of heat pipes. However, Kim price. The outcomes and co-authors innew studied heat exchangers with parallel flow with collectors, which are show that the [10] style meets the decomposition temperature requirements and increases thein several industries due to their compact of heat pipes. Around the broadly utilized heat flow rate, and validates the use size and ease of application. They other hand, Kim and co-authors in to understand heat exchangers with parallel flowdistribution and carried out analysis [10] studied flow qualities and increase flow with collectors, that are extensively.