T to decide the manage strategy of the program in true conditions. Figures 12 and

T to decide the manage strategy of the program in true conditions. Figures 12 and 13 show the heat transfer coefficients (k , r) and heat flux density on the thermally activated ceiling (qk , qr) by introducing discrete steady states for any Benzamide Cancer complete test cycle (24 h) and separating the period of regeneration of the phase modify material plus the period of occurrence in the cooling load. The figures had been developed determined by the outcomes collected for variants Ia IIb. The parameters describing the convective heat transfer (qk , k) have been presented based on the temperature distinction involving the surface of your ceiling with PCM and the air. Parameters describing radiative heat transfer (qr , r) had been presented as a function with the temperature distinction involving the PCM ceiling surface and the other thermally non-activated surfaces. The selection of the temperature difference shown in the figures corresponds to the operating situations with the system for the analyzed variants. Higher temperature differences have been obtained for the duration of the regeneration time.2021, 14, x FOR PEER Overview PEER Overview Energies 2021, 14, x FOR13 of13 ofshown Energies 2021, 14,inside the figures corresponds towards the operating circumstances with the system forthe program for the anashown within the figures corresponds for the operating circumstances with the ana13 of 16 lyzed variants. Greater temperature differences had been obtainedwere obtained during the regeneration during the regeneration lyzed variants. Larger temperature variations time. time.Figure 12. Propaquizafop Cancer Quasi-steady-state conditions–activation timetime and operate hours. Figure 12. Quasi-steady-state conditions–activation time and operate hours.perform hours. Figure 12. Quasi-steady-state conditions–activation and(a)(a)(b)(b)Figure 13. Quasi-steady-state conditions–(a) activation time c, (b) operate time c, (b) work hours. hours. Figure 13. Quasi-steady-state conditions–(a) activation time c, (b) perform hours. Figure 13. Quasi-steady-state conditions–(a) activationTable three presents the heat transfer coefficient andcoefficientdensity asflux densitytem- as function of Table 3 presents the heat transfer heat flux and heat function of as function of tem3 presents the heat transfer coefficient and heat flux density perature difference involving a thermally activated surface and air surface andairT) or perature difference in between a thermally activated surface and air(convection, Tc)) or temperature distinction in between a thermally activated (convection, (convection, T non-activated surfaces (radiation, T (radiation, T). non-activated surfaces). TrTable three. Equations proposed for the calculation of heat flux density andflux density and heat transfer coefficient. Table 3. Equations proposed for the calculation of heat flux density and heat transfer coefficient. of heat heat transfer coefficient.Activation Time ActivationTime Perform Hours Operate Hours Activation Time Perform Hours . . Convective heat flux density flux = 1.8297 = 1.8297 = 1.8234 = 1.8234 1.2769 q density q . Convectiveheat flux density heat q = 1.8297 1.3347 q q = 1.8234 . qc Convective c c (R2 = 0.9978) (R2 = 0.9978) (R2 = 0.9995) c (R22= 0.9995) [W/m2] [W/m [W/m2 ]2] (R2 = 0.9978) (R = 0.9995) . . Radiant heat flux density flux density q = 11.419 = 11.419 = 11.379 = 11.379 1.005 q . Radiant heat q q q = 11.379 . Radiant heat flux density (R2 = 1) qr = 11.419 r 0.9927 r two = 1) 2] r (R [W/m (R2 = 1) (R22= 1) [W/m2 [W/m2 ] ] (R2 = 1) (R = 1) . . Convective heat transfer coeffi-transfer1.8297 = 1.8297 = 1.