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MTR(E), MTC, MTA - Grundfos

MTR(E), MTC, MTA - Grundfos

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2<br />

<strong>MTC</strong><br />

70<br />

Minimum inlet pressure - NPSHR<br />

Calculation of the inlet pressure "H" is recommended<br />

when ....<br />

• the liquid temperature is high,<br />

• the flow is significantly higher than the rated flow,<br />

• inlet conditions are poor.<br />

To avoid cavitation, make sure that there is a minimum<br />

pressure on the suction side of the pump. The<br />

maximum suction lift "H" in feet of head can be<br />

calculated as follows:<br />

H = pb – NPSHR – Hf – Hv – Hs pb = Barometric pressure in feet absolute.<br />

(Barometric pressure can be set to 33.9<br />

feet).<br />

In closed systems, pb indicates the system<br />

pressure in feet.<br />

NPSHR = Net Positive Suction Head in feet of head.<br />

(To be read from the NPSHR curve at the<br />

highest flow rate the pump will be<br />

delivering).<br />

H f<br />

H v<br />

= Friction loss in suction pipe in feet of head.<br />

(At the highest flow rate the pump will be<br />

delivering.)<br />

= Vapor pressure in feet.<br />

(To be read from the vapor pressure scale.<br />

"H v " depends on the liquid temperature<br />

"T m ").<br />

Hs = Safety margin = minimum 2.0 feet.<br />

If the "H" calculated is positive, the pump can operate<br />

at a suction lift of maximum "H" feet of head.<br />

If the "H" calculated is negative, an inlet pressure of<br />

minimum "H" feet of head is required.<br />

H f<br />

P b<br />

Fig. 43 Minimum inlet pressure - NPSHR<br />

<strong>MTR</strong>(E), <strong>MTC</strong>, <strong>MTA</strong><br />

tm<br />

(°F)<br />

Hv<br />

(Ft)<br />

370 413<br />

360 328<br />

340 259<br />

320 203<br />

250 66<br />

230 49<br />

39<br />

212 33<br />

194<br />

26<br />

20<br />

176 16<br />

13<br />

158 10<br />

140 6.6<br />

122<br />

4.9<br />

3.3<br />

104 2.6<br />

2.0<br />

86 1.3<br />

0.9<br />

68<br />

0.7<br />

50<br />

32<br />

0.3<br />

Note: In order to avoid cavitation, never select a pump<br />

whose duty point is too far to the right on the NPSHR<br />

curve.<br />

Always check the NPSHR value of the pump at the<br />

highest possible flow rate.<br />

Q<br />

H<br />

H v<br />

300<br />

280<br />

270<br />

148<br />

131<br />

115<br />

98<br />

82<br />

TM03 4307 2006

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