Technische fiche - Delta-Temp

BT08L005GB-01PACKAGED362 - 904THERMODYNAMIC ENERGY RECOVERY AND CONSUMPTION REDUCTION SOURCE SIDECOOLING PERFORMANCETHERMODYNAMIC RECOVERY ACTIVE WITH 15% 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)667 6,63 0,32 8,07 0,39 10,74 0,51 13,57 0,65 16,58 0,79833 8,02 0,38 9,76 0,47 12,84 0,61 16,24 0,78 19,87 0,951000 9,47 0,45 11,53 0,55 15,10 0,72 19,10 0,91 23,38 1,12733 7,30 0,35 8,88 0,42 11,82 0,57 14,93 0,71 18,24 0,87917 8,82 0,42 10,73 0,51 14,13 0,68 17,87 0,85 21,86 1,051083 10,26 0,49 12,49 0,60 16,36 0,78 20,69 0,99 25,33 1,21800 7,92 0,38 9,64 0,46 12,90 0,62 16,30 0,78 19,90 0,951000 9,59 0,46 11,70 0,56 15,40 0,74 19,60 0,94 23,90 1,141125 10,60 0,51 12,90 0,62 17,00 0,81 21,50 1,03 26,30 1,26958 9,54 0,46 11,61 0,56 15,44 0,74 19,52 0,93 23,84 1,141208 11,63 0,56 14,15 0,68 18,62 0,89 23,55 1,13 28,81 1,381458 13,82 0,66 16,82 0,80 22,02 1,05 27,86 1,33 34,10 1,631083 10,78 0,52 13,12 0,63 17,46 0,84 22,06 1,06 26,95 1,291354 13,03 0,62 15,86 0,76 20,87 1,00 26,39 1,26 32,29 1,541625 15,40 0,74 18,74 0,90 24,54 1,17 31,04 1,49 37,99 1,821208 12,03 0,58 14,64 0,70 19,47 0,93 24,61 1,18 30,06 1,441500 14,43 0,69 17,57 0,84 23,12 1,11 29,24 1,40 35,76 1,711750 16,58 0,79 20,18 0,97 26,43 1,26 33,43 1,60 40,92 1,961333 13,27 0,63 16,15 0,77 21,49 1,03 27,15 1,30 33,17 1,591667 16,04 0,77 19,52 0,93 25,69 1,23 32,48 1,55 39,74 1,901833 17,37 0,83 21,14 1,01 27,68 1,32 35,02 1,68 42,87 2,051500 14,93 0,71 18,17 0,87 24,17 1,16 30,55 1,46 37,32 1,791875 18,04 0,86 21,96 1,05 28,90 1,38 36,55 1,75 44,70 2,142208 20,92 1,00 25,47 1,22 33,35 1,60 42,18 2,02 51,63 2,471667 16,59 0,79 20,19 0,97 26,86 1,29 33,94 1,62 41,46 1,982083 20,04 0,96 24,40 1,17 32,11 1,54 40,60 1,94 49,67 2,382333 22,11 1,06 26,91 1,29 35,23 1,69 44,57 2,13 54,56 2,61The 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 30% OF EXPELLED /FRESH AIR32Size362402452464524604704804904Qo(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)1333 31,50 1,51 30,78 1,47 29,44 1,41 28,95 1,39 27,89 1,33 26,72 1,281667 32,77 1,57 32,01 1,53 30,67 1,47 30,08 1,44 28,99 1,39 27,75 1,332000 35,79 1,71 34,96 1,67 33,54 1,60 32,84 1,57 31,66 1,51 30,29 1,451466 34,65 1,66 33,85 1,62 32,38 1,55 31,84 1,52 30,68 1,47 29,39 1,411833 36,05 1,72 35,22 1,68 33,74 1,61 33,09 1,58 31,90 1,53 30,53 1,462167 38,78 1,86 37,88 1,81 36,34 1,74 35,58 1,70 34,30 1,64 32,81 1,571600 37,82 1,81 36,94 1,77 35,29 1,69 34,68 1,66 33,38 1,60 32,04 1,532000 39,49 1,89 38,58 1,85 36,95 1,77 36,16 1,73 34,82 1,67 33,4 1,602250 40,29 1,93 39,34 1,88 37,67 1,80 36,86 1,76 35,48 1,70 34,04 1,631917 45,29 2,17 44,25 2,12 42,32 2,03 41,62 1,99 40,10 1,92 38,41 1,842417 47,52 2,27 46,42 2,22 44,48 2,13 43,62 2,09 42,05 2,01 40,25 1,932917 52,20 2,50 50,99 2,44 48,91 2,34 47,89 2,29 46,17 2,21 44,17 2,112167 51,19 2,45 50,02 2,39 47,84 2,29 47,04 2,25 45,33 2,17 43,42 2,082708 53,26 2,55 52,02 2,49 49,85 2,39 48,89 2,34 47,12 2,25 45,10 2,163250 58,17 2,78 56,82 2,72 54,50 2,61 53,37 2,55 51,45 2,46 49,22 2,362417 57,10 2,73 55,79 2,67 53,37 2,55 52,47 2,51 50,57 2,42 48,43 2,323000 58,99 2,82 57,63 2,76 55,22 2,64 54,15 2,59 52,20 2,50 49,96 2,393500 62,65 3,00 61,20 2,93 58,70 2,81 57,48 2,75 55,41 2,65 53,01 2,542667 63,01 3,01 61,56 2,95 58,89 2,82 57,90 2,77 55,79 2,67 53,44 2,563333 65,54 3,14 64,03 3,06 61,35 2,94 60,17 2,88 57,99 2,77 55,51 2,663667 65,63 3,14 64,11 3,07 61,49 2,94 60,21 2,88 58,04 2,78 55,53 2,663000 70,88 3,39 69,25 3,31 66,25 3,17 65,14 3,12 62,77 3,00 60,12 2,883750 73,74 3,53 72,03 3,45 69,02 3,30 67,69 3,24 65,24 3,12 62,45 2,994417 79,05 3,78 77,22 3,69 74,07 3,54 72,53 3,47 69,92 3,35 66,89 3,203333 78,76 3,77 76,95 3,68 73,61 3,52 72,37 3,46 69,74 3,34 66,80 3,204166 81,92 3,92 80,03 3,83 76,69 3,67 75,21 3,60 72,49 3,47 69,38 3,324667 83,53 4,00 81,59 3,90 78,27 3,74 76,64 3,67 73,88 3,53 70,68 3,38The 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°C