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DN mm |
Kvs m³/h |
dPmax bar |
L mm |
Xp °C |
Tc seс |
dT °C |
price |
---|---|---|---|---|---|---|---|
15 | 0.40 1.0 2.5 3.2 |
8 | 65 | - | - | 0 - 35 25 - 70 40 - 100 50 - 120 70 - 150 |
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20 | 4.0 |
8 | 75 | - | - | 0 - 35 25 - 70 40 - 100 50 - 120 70 - 150 |
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25 | 5.0 |
8 | 90 | - | - | 0 - 35 25 - 70 40 - 100 50 - 120 70 - 150 |
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32 | 10 |
8 | 100 | - | - | 0 - 35 25 - 70 40 - 100 50 - 120 70 - 150 |
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40 | 13 |
8 | 110 | - | - | 0 - 35 25 - 70 40 - 100 50 - 120 70 - 150 |
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50 | 16 |
8 | 130 | - | - | 0 - 35 25 - 70 40 - 100 50 - 120 70 - 150 |
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DN - nominal diameter, mm.
Тс - time constant, sec.
L - length along the pipeline axis, mm.
dT - range of temperatures maintained by the controller, °C.
dPmax - maximum pressure drop across the controller, bar.
Xp - proportional band corresponds to the temperature deviation in °C from the setpoint at which the valve of the controller will go to the extreme position.
Kvs - flow coefficient, corresponds to the water flow rate in m³/h at which the pressure drop across the controller will be 1 bar.
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