Technische fiche - Delta-Temp

BT08L005GB-01PACKAGED362 - 904HEATING PERFORMANCETHERMODYNAMIC RECOVERY ACTIVE WITH 30% OF EXPELLED /FRESH AIRSize362402452464524604704804904Qo(l/s)Return air temperature (D.B.) relative humidity of return air14 °C 50% U.R. 16 °C 50% U.R. 18 °C 50% U.R. 20 °C 50% U.R. 22 °C 50% U.R.P (kW) Qa (l/s) P (kW) Qa (l/s) P (kW) Qa (l/s) P (kW) Qa (l/s) P (kW) Qa (l/s)1333 11,75 0,56 14,33 0,69 18,42 0,88 23,33 1,12 28,58 1,371667 13,92 0,67 17,00 0,81 21,50 1,03 27,33 1,31 33,42 1,602000 16,18 0,77 19,82 0,95 24,80 1,19 31,55 1,51 38,57 1,851466 12,92 0,62 15,76 0,75 20,26 0,97 25,66 1,23 31,44 1,501833 15,31 0,73 18,70 0,89 23,65 1,13 30,07 1,44 36,76 1,762167 17,53 0,84 21,47 1,03 26,87 1,29 34,18 1,64 41,79 2,001600 14,10 0,67 17,20 0,82 22,10 1,06 28,00 1,34 34,30 1,642000 16,70 0,80 20,40 0,98 25,80 1,23 32,80 1,57 40,10 1,922250 18,20 0,87 22,30 1,07 27,90 1,33 35,50 1,70 43,40 2,081917 16,89 0,81 20,61 0,99 26,48 1,27 33,54 1,60 41,09 1,972417 20,18 0,97 24,65 1,18 31,18 1,49 39,64 1,90 48,46 2,322917 23,59 1,13 28,91 1,38 36,17 1,73 46,02 2,20 56,26 2,692167 19,09 0,91 23,29 1,11 29,93 1,43 37,92 1,81 46,45 2,222708 22,62 1,08 27,63 1,32 34,94 1,67 44,42 2,13 54,31 2,603250 26,29 1,26 32,21 1,54 40,30 1,93 51,28 2,45 62,69 3,002417 21,30 1,02 25,98 1,24 33,38 1,60 42,30 2,02 51,81 2,483000 25,05 1,20 30,60 1,46 38,70 1,85 49,20 2,35 60,16 2,883500 28,31 1,35 34,69 1,66 43,40 2,08 55,22 2,64 67,51 3,232667 23,50 1,12 28,67 1,37 36,84 1,76 46,67 2,23 57,17 2,743333 27,84 1,33 34,00 1,63 43,00 2,06 54,67 2,62 66,84 3,203667 29,66 1,42 36,34 1,74 45,47 2,18 57,85 2,77 70,72 3,383000 26,44 1,27 32,25 1,54 41,44 1,98 52,50 2,51 64,32 3,083750 31,32 1,50 38,25 1,83 48,38 2,31 61,51 2,94 75,20 3,604417 35,73 1,71 43,77 2,09 54,77 2,62 69,68 3,33 85,19 4,083333 29,38 1,41 35,84 1,71 46,04 2,20 58,34 2,79 71,46 3,424166 34,79 1,66 42,50 2,03 53,75 2,57 68,34 3,27 83,54 4,004667 37,75 1,81 46,25 2,21 57,87 2,77 73,63 3,52 90,02 4,31The table shows the benefits of the thermodynamic recoverer in terms of reduction of power exchanged with the source and of reduction of the water flow on the source side (ex. WLHPloop). They do not represent an additional increase of the machine's power, whose general performance remain basically unchanged if compared to the models without such option.Qo = expelled air flow rate (l/s)P = power due to the heat exchange on the recovery coil which relieves the source side (water loop) in kWQa = reduction of water flow rate due to thermal exchange on the recovery coil which relieves the plate exchanger on the water loop side (l/s)The yields of the recovery and the calculation of the reduction of water flow rate refer to a loop with water entering the exchanger at 15°C and leaving it at 10°CTHERMODYNAMIC RECOVERY ACTIVE WITH 45% OF EXPELLED /FRESH AIRSize362402452464524604704804904Qo(l/s)Return air temperature (D.B.) relative humidity of return air22 °C 50% U.R. 25 °C 50% U.R. 27 °C 50% U.R. 28 °C 50% U.R. 30 °C 50% U.R. 32 °C 50% U.R.P (kW) Qa (l/s) P (kW) Qa (l/s) P (kW) Qa (l/s) P (kW) Qa (l/s) P (kW) Qa (l/s) P (kW) Qa (l/s)2000 33,94 1,62 33,18 1,59 31,66 1,51 31,07 1,49 29,89 1,43 28,63 1,372500 34,79 1,66 34,13 1,63 32,51 1,56 31,92 1,53 30,69 1,47 29,38 1,413000 37,67 1,80 37,04 1,77 35,24 1,69 34,62 1,66 33,27 1,59 31,83 1,522200 37,33 1,79 36,50 1,75 34,83 1,67 34,18 1,64 32,87 1,57 31,49 1,512750 38,27 1,83 37,55 1,80 35,77 1,71 35,12 1,68 33,76 1,62 32,32 1,553250 40,81 1,95 40,13 1,92 38,18 1,83 37,50 1,79 36,04 1,72 34,49 1,652400 40,70 1,95 39,73 1,90 38,04 1,82 37,21 1,78 35,83 1,71 34,36 1,643000 41,46 1,98 40,97 1,96 39,18 1,87 38,32 1,83 36,88 1,76 35,36 1,693375 42,36 2,03 41,54 1,99 39,71 1,90 38,83 1,86 37,37 1,79 35,82 1,712875 48,79 2,33 47,70 2,28 45,52 2,18 44,67 2,14 42,97 2,06 41,16 1,973625 50,45 2,41 49,50 2,37 47,15 2,26 46,30 2,22 44,51 2,13 42,60 2,044375 54,94 2,63 54,02 2,58 51,40 2,46 50,49 2,42 48,52 2,32 46,43 2,223250 55,15 2,64 53,92 2,58 51,45 2,46 50,50 2,42 48,57 2,32 46,52 2,234063 56,54 2,71 55,47 2,65 52,84 2,53 51,88 2,48 49,88 2,39 47,75 2,284875 61,22 2,93 60,19 2,88 57,28 2,74 56,25 2,69 54,06 2,59 51,73 2,483625 61,52 2,94 60,15 2,88 57,40 2,75 56,33 2,70 54,18 2,59 51,89 2,484500 62,62 3,00 61,44 2,94 58,53 2,80 57,47 2,75 55,25 2,64 52,89 2,535250 65,93 3,15 64,82 3,10 61,68 2,95 60,59 2,90 58,22 2,79 55,72 2,674000 67,88 3,25 66,37 3,18 63,33 3,03 62,15 2,97 59,78 2,86 57,26 2,745000 69,58 3,33 68,27 3,27 65,03 3,11 63,85 3,06 61,38 2,94 58,76 2,815500 69,07 3,30 67,91 3,25 64,62 3,09 63,47 3,04 60,99 2,92 58,37 2,794500 76,36 3,65 74,66 3,57 71,25 3,41 69,92 3,35 67,25 3,22 64,42 3,085625 78,28 3,75 76,80 3,67 73,16 3,50 71,84 3,44 69,06 3,30 66,11 3,166625 83,19 3,98 81,80 3,91 77,84 3,72 76,45 3,66 73,47 3,52 70,31 3,365000 84,85 4,06 82,96 3,97 79,16 3,79 77,69 3,72 74,73 3,58 71,57 3,426250 86,97 4,16 85,33 4,08 81,29 3,89 79,81 3,82 76,72 3,67 73,45 3,517000 87,91 4,21 86,43 4,14 82,25 3,94 80,78 3,87 77,63 3,71 74,29 3,55The table shows the benefits of the thermodynamic recoverer in terms of reduction of power exchanged with the source and of reduction of the water flow on the source side (ex. WLHPloop). They do not represent an additional increase of the machine's power, whose general performance remain basically unchanged if compared to the models without such option.Qo = expelled air flow rate (l/s)P = power due to the heat exchange on the recovery coil which relieves the source side (water loop) in kWQa = reduction of water flow rate due to thermal exchange on the recovery coil which relieves the plate exchanger on the water loop side (l/s)The yields of the recovery and the calculation of the reduction of water flow rate refer to a loop with water entering the exchanger at 15°C and leaving it at 10°C34