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 Overview Energies 2021, 14, x FOR32 of 38 34 of(a) Fluid velocity in Figure 33. (a) Fluid velocity inside the total heat pipe and in the condenser section, (b) the volume fraction of steam inside the total heat pipe and in the evaporator section.14, xx FOR PEER Critique 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 of the heat heat pipe’s central line. Temperature distribution along along the on 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.4, x FOR PEER REVIEWEnergies 2021, 14,36 of34 ofFigure 36. Temperature distribution along the height from the heat pipe’s wall. Figure 36. Temperature distribution along the height of the heat pipe’s wall.4. Discussion4. Discussion Numerical strategies of studying Heat Pipes are usually not the subject of quite a few scientists’Numerical solutions of studying Heat Pipes are certainly not the subject of many scientists’ function, mostly as a result of complexity of the processes taking place inside them at the very same operate, mainly duetime. In their analysis, the processes taking place[7] built them in the very same of a heat towards the complexity of Chen along with other co-authors inside a theoretical model time. In their analysis,the outcomes of that are similar[7] the results presentedmodel of a heat On the pipe, Chen as well as other co-authors to constructed a theoretical in this publication. pipe, the results of which areQian [8] presented a three-dimensional numerical modelOn theon comparable other hand, equivalent towards the outcomes presented within this publication. based other hand, Qian numerical assumptions presented in this publication. In Ref. [9],on similarco-authors [8] presented a three-dimensional numerical model primarily based Gao and focused on the structural publication. In Ref. zone of and co-authors fonumerical assumptions presented in this DMPO medchemexpress decomposition plant. style with the tube was zone of your sulfuric acid in the heat transfer cused around the structuralThe double inner catalytic developed 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 from the heat transfer price. The results show that the new style meets the decomposition temperature needs and surface in the inner tube as well as the catalytic volume in the ring location around the decomposition increases the heat flow rate, and validates the usage of heat pipes. On the other hand, 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 needs and increases thein various industries as a consequence of their compact of heat pipes. On the extensively employed heat flow price, 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 performed research [10] studied flow characteristics and enhance flow with collectors, which are broadly.
