Thermostatic expansion valves TUA/TUAE

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Technical brochure Thermostatic expansion valves, type TUA/TUAE Ordering (continued) Orifice assembly with filter and gasket. Range N: –40 → +10°C Orifice no. Rated capacity in kW 1) Rated capacity in tons (TR) 1) Code no. R22 R134a R404A R407C R507 R410A R22 R134a R404A R407C R507 R410A 0 0.60 0.47 0.47 0.63 0.45 - 0.17 0.13 0.13 0.18 0.13 - 068U1030 1 0.9 0.7 0.70 0.92 0.66 1.3 0.25 0.19 0.19 0.26 0.19 0.4 068U1031 2 1.3 1.0 1.0 1.4 1.0 2.1 0.36 0.28 0.28 0.38 0.27 0.6 068U1032 3 1.8 1.4 1.4 1.9 1.3 2.9 0.50 0.39 0.39 0.53 0.38 0.8 068U1033 4 2.6 2.1 2.1 2.8 2.0 4.5 0.75 0.59 0.60 0.80 0.57 1.3 068U1034 5 3.5 2.7 2.8 3.8 2.7 5.9 1.00 0.78 0.79 1.1 0.76 1.7 068U1035 6 5.3 4.1 4.2 5.7 4.0 9.0 1.5 1.2 1.2 1.6 1.1 2.5 068U1036 7 7.0 5.5 5.6 7.5 5.3 12.0 2.0 1.6 1.6 2.1 1.5 3.4 068U1037 8 11.0 8.2 8.4 11.0 8.0 18.0 3.0 2.3 2.4 3.2 2.3 5.0 068U1038 9 16.0 12.0 12.0 17.0 12.0 26.0 4.5 3.5 3.5 4.8 3.4 7.5 068U1039 Range B: –60 → –25°C 1 ) Rated capacity Q nom. is based on: Evaporating temperature t e = +5°C for range N and – 30°C for range B Condensing temperature t c = +32°C Refrigerant liquid temperature t l = +28°C Opening superheat OS = 4 K Orifice no. Rated capacity in kW 1) Rated capacity in tons (TR) 1) Code no. R22 R404A R407C R507 R22 R404A R407C R507 0 0.52 0.36 0.46 0.39 0.15 0.10 0.13 0.11 068U1030 1 0.68 0.50 0.58 0.53 0.19 0.14 0.16 0.15 068U1031 2 0.85 0.64 0.70 0.70 0.24 0.18 0.20 0.20 068U1032 3 1.2 0.89 1.0 1.0 0.34 0.25 0.28 0.28 068U1033 4 1.8 1.3 1.4 1.4 0.50 0.37 0.41 0.41 068U1034 5 2.3 1.8 1.9 1.9 0.66 0.50 0.55 0.55 068U1035 6 3.5 2.7 2.9 2.9 1.0 0.75 0.82 0.82 068U1036 7 4.7 3.5 3.9 3.9 1.3 1.0 1.1 1.1 068U1037 8 7.1 5.3 5.8 5.8 2.0 1.5 1.6 1.7 068U1038 9 10.4 7.8 8.5 8.6 2.9 2.2 2.4 2.4 068U1039 Spare parts Gasket (24 pcs.): 068U0015 Note: to ensure tightness the orifice gasket must be exchanged each time the orifice assembly is unscrewed. Filter (24 pcs.): 068U0016 6 DKRCC.PD.AG0.A3.02 / 520H4543 © Danfoss A/S (AG-SMC / bpv), 07 - 2010
Technical brochure Thermostatic expansion valves, type TUA/TUAE Capacity Capacity in kW for range N = −40 → +10°C and opening superheat OS = 4 K Valve type TU TU TU Orifice no. 0 1 2 3 4 5 6 7 8 9 0 1 2 3 4 5 6 7 8 9 0 1 2 3 4 5 6 7 8 9 Pressure drop across valve ∆p bar Pressure drop across valve ∆p bar 2 4 6 8 10 12 14 16 2 4 6 8 10 12 14 16 0.42 0.61 0.9 1.2 1.8 2.4 3.7 4.9 7.3 10.9 0.36 0.47 0.60 0.8 1.2 1.7 2.5 3.3 5.0 7.4 0.53 0.79 1.2 1.6 2.4 3.2 4.9 6.5 9.6 14.5 0.46 0.62 0.78 1.1 1.6 2.2 3.2 4.3 6.5 9.7 0.34 0.39 0.47 0.66 1.0 1.3 1.9 2.6 3.9 5.7 Evaporating temperature +10°C Evaporating temperature 0°C 0.60 0.89 1.3 1.8 2.8 3.7 5.6 7.5 11.2 16.7 0.65 1.0 1.5 2.0 3.1 4.1 6.1 8.2 12.2 18.2 0.68 1.0 1.6 2.1 3.2 4.3 6.5 8.6 12.9 19.3 0.70 1.0 1.6 2.2 3.4 4.5 6.7 9.0 13.4 20.0 Evaporating temperature –10°C 0.51 0.70 0.89 1.3 1.9 2.5 3.7 5.0 7.5 11.1 0.55 0.75 1.0 1.4 2.0 2.7 4.0 5.4 8.1 12.0 0.57 0.79 1.0 1.4 2.1 2.8 4.3 5.7 8.5 12.6 0.59 0.81 1.1 1.5 2.2 2.9 4.4 5.9 8.8 13.1 Evaporating temperature –30°C 0.38 0.45 0.53 0.74 1.1 1.5 2.2 2.9 4.4 6.5 0.40 0.48 0.57 0.80 1.2 1.6 2.4 3.2 4.8 7.0 0.42 0.51 0.60 0.84 1.2 1.7 2.5 3.3 5.0 7.3 0.44 0.52 0.62 0.87 1.3 1.7 2.5 3.4 5.1 7.5 0.71 1.1 1.7 2.3 3.5 4.6 6.9 9.2 13.7 20.5 0.60 0.82 1.1 1.5 2.2 3.0 4.5 6.0 9.0 13.3 0.44 0.53 0.63 0.88 1.3 1.7 2.6 3.5 5.2 7.7 0.72 1.1 1.7 2.3 3.5 4.7 7.1 9.4 13.9 20.9 0.61 0.83 1.1 1.5 2.3 3.0 4.6 6.1 9.1 13.5 0.45 0.54 0.63 0.89 1.3 1.8 2.6 3.5 5.3 7.7 0.40 0.55 0.73 1.0 1.5 2.0 3.1 4.1 6.1 9.1 0.50 0.71 1.0 1.3 2.0 2.7 4.0 5.4 8.0 12.1 0.40 0.51 0.61 0.9 1.3 1.7 2.5 3.4 5.1 7.6 0.56 0.80 1.1 1.5 2.3 3.1 4.6 6.2 9.2 13.8 0.60 0.86 1.2 1.7 2.5 3.4 5.0 6.7 10.1 15.0 0.63 0.91 1.3 1.8 2.7 3.5 5.3 7.1 10.6 15.9 0.65 0.93 1.3 1.8 2.8 3.7 5.5 7.4 11.0 16.4 Evaporating temperature –20°C 0.45 0.57 0.70 1.0 1.5 1.9 2.9 3.9 5.8 8.6 0.48 0.62 0.76 1.1 1.6 2.1 3.1 4.2 6.3 9.3 0.50 0.65 0.79 1.1 1.6 2.2 3.3 4.4 6.6 9.7 0.52 0.67 0.82 1.2 1.7 2.3 3.4 4.5 6.8 10.1 Evaporating temperature –40°C 0.31 0.33 0.39 0.55 0.80 1.1 1.6 2.1 3.2 4.7 0.33 0.36 0.42 0.59 0.86 1.2 1.7 2.3 3.5 5.1 0.34 0.38 0.44 0.61 0.90 1.2 1.8 2.4 3.6 5.3 0.35 0.39 0.45 0.63 0.92 1.2 1.8 2.5 3.7 5.5 0.67 0.95 1.4 1.9 2.8 3.8 5.7 7.6 11.3 16.8 0.53 0.68 0.84 1.2 1.7 2.3 3.5 4.6 7.0 10.3 0.36 0.39 0.46 0.64 0.94 1.3 1.9 2.5 3.8 5.5 R22 0.67 0.96 1.4 1.9 2.8 3.8 5.8 7.7 11.5 17.1 0.53 0.69 0.85 1.2 1.8 2.3 3.5 4.7 7.1 10.4 0.36 0.40 0.46 0.65 0.95 1.3 1.9 2.5 3.8 5.6 Correction for subcooling ∆t sub The evaporator capacity used must be corrected if subcooling deviates from 4 K. The corrected capacity can be obtained by dividing the evaporator capacity by the correction factor given below. Note: Insufficient subcooling can produce flash gas. Correction factor for subcooling ∆t sub ∆t sub 4 K 10 K 15 K 20 K 25 K 30 K 35 K 40 K 45 K 50 K Correction factor 1.00 1.06 1.11 1.15 1.2 1.25 1.3 1.35 1.39 1.44 Selection example Refrigerant = R22 Evaporating temperature t e = −10°C Pressure drop in valve ∆p = 10 bar Subcooling ∆t sub = 15 K Evaporator capacity = 3 kW Correction value (table) = 1.11 The corrected evaporator capacity thus becomes 3 divided by 1.11 = 2.7 kW Since the expansion valve capacity must be equal to or slightly more than the corrected evaporator capacity of 2.7 kW, a TUB/TUBE with orifice 5 and a table capacity of 2.8 kW would be a suitable choice. © Danfoss A/S (AG-SMC / bpv), 07 - 2010 DKRCC.PD.AG0.A3.02 / 520H4543 7
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Thermostatic expansion valves TUA/TUAE

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