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2921 Scheda tecnica(PDF) 12 Page - Christian Bürkert GmbH & Co. KG |
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2921 Scheda tecnica(HTML) 12 Page - Christian Bürkert GmbH & Co. KG |
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12 / 17 page ![]() Type 2961 12 | 17 Visit product website 5. Performance specifications 5.1. Fluidic data Flow characteristics • Flow characteristic according to DIN EN 60534 - 2 - 4 • K VR value at 5 % of stroke for DN > 10 mm K VR value at 10 % of stroke for DN ≤ 10 mm • K VR value = smallest KV value, at which the tilt tolerance according to DIN EN 60534 - 2 - 4 is still maintained. 100 90 80 70 60 50 40 30 20 10 0 0 10 20 30 40 50 60 70 80 90 100 Stroke [%] Equal percentage flow curve - detailed values please see below Overview of fluidic data for flow below seat (for liquids, steam and gases) Note: • K V value [m 3 /h]: measurement with water according to DIN EN 60534 - 2 - 4 • Seat leakage according to DIN EN 60534 - 4 • Bürkert product filter(see “7.2. Bürkert product filter” on page 17) • Info: Rules for decimal places implemented according to works standard Nominal diameter (pipe) Seat size Hand- wheel dia- meter Ø Operating pressure max. CF A (Seat leakage class) Theo- retical range- ability K V value at stroke [m 3 /h] K VS value Seat seal Stain- less steel PTFE PEEK DN NPS [mm] [bar(g)] 5 % 10 % 20 % 30 % 40 % 50 % 60 % 70 % 80 % 90 % 100 % [m3/h] 10 ¾ 1.) 3 45 (S) 25 (II) – – 10:1 – 0.005 0.009 0.013 0.019 0.026 0.034 0.044 0.060 0.077 0.098 0.1 3 45 (S) 25 (II) 20:1 – 0.009 0.015 0.023 0.033 0.046 0.063 0.085 0.11 0.16 0.22 0.2 4 45 (S) 25 (II) 30:1 – 0.023 0.033 0.049 0.070 0.097 0.14 0.18 0.26 0.35 0.49 0.5 6 45 (S) 25 (II) 25 (VI) 25 (VI) 50:1 0.005 0.007 0.011 0.045 0.085 0.16 0.26 0.41 0.65 1.1 1.25 1.25 8 45 (S) 25 (II) 25 (VI) 25 (VI) 0.060 0.070 0.090 0.12 0.18 0.26 0.42 0.61 0.92 1.5 2.0 2.0 10 45 (S) 25 (II) 25 (VI) 25 (VI) 0.090 0.11 0.13 0.19 0.30 0.48 0.73 1.0 1.6 2.3 2.7 2.7 15 ½2.) 3 45 (S) 25 (II) – – 10:1 – 0.005 0.009 0.013 0.019 0.026 0.034 0.044 0.060 0.077 0.098 0.1 3 45 (S) 25 (II) 20:1 – 0.009 0.015 0.023 0.033 0.046 0.063 0.085 0.11 0.16 0.22 0.2 4 45 (S) 25 (II) 30:1 – 0.023 0.033 0.049 0.070 0.097 0.14 0.18 0.26 0.35 0.49 0.5 6 45 (S) 25 (II) 25 (VI) 25 (VI) 50:1 0.005 0.007 0.011 0.045 0.085 0.16 0.26 0.41 0.65 1.1 1.25 1.25 8 45 (S) 25 (II) 25 (VI) 25 (VI) 0.070 0.080 0.11 0.13 0.19 0.27 0.43 0.63 0.95 1.6 2.1 2.1 10 45 (S) 25 (II) 25 (VI) 25 (VI) 0.090 0.11 0.15 0.19 0.31 0.49 0.75 1.1 1.7 2.5 3.1 3.1 15 45 (S) 25 (II) 25 (VI) 25 (VI) 0.14 0.17 0.22 0.35 0.52 0.80 1.2 1.8 2.7 3.7 4.3 4.3 20 ¾2.) 10 45 (S) 25 (II) 25 (VI) 25 (VI) 50:1 0.10 0.12 0.15 0.19 0.30 0.46 0.67 1.0 1.5 2.1 2.8 2.8 15 45 (S) 25 (II) 25 (VI) 25 (VI) 0.13 0.17 0.21 0.32 0.48 0.71 1.0 1.5 2.3 3.4 4.4 4.4 20 45 (S) 25 (II) 25 (VI) 25 (VI) 0.19 0.24 0.29 0.42 0.64 0.97 1.4 2.0 2.9 4.2 5.9 5.9 1.) Deviation for port connections according to ASME BPE: the next largest Nominal diameter (port connection) is used, e.g. NPS 1 instead of NPS ¾. 2.) According to the Pressure Equipment Directive 97/23/EC for compressible fluids of Group 1 (hazardous gases and vapours according to Article 3 No. 1.3 letter a first dash) |
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