FK 40 - Tri-Canada
FK 40 - Tri-Canada FK 40 - Tri-Canada
Positive displacement pumps Case 1: viscosity η ∪ 1 mPa s Step 3: Calculate t he power N [kW] required f or t he pump drive. p = pressure [bar] V = viscosity factor n = speed [1/min], stated in the diagram C = flow rate/revolution [l/rev.] Example:
Example: Q = 3000 l/h H = 120 m ∪ p = 12 bar η = 10 mPa s Step 1: speed correction stated in the diagram: p = 3.8 bar. Def ine now t he speed required f or t he correct ed pressure. Positive displacement pumps Case 2: viscous product η up to 200 mPa s
- Page 2 and 3: Content Pump technology terms . . .
- Page 4 and 5: Pump technology terms Flow rat e [m
- Page 6 and 7: Pump technology terms Flow behaviou
- Page 8 and 9: Pump technology terms Types of flow
- Page 10 and 11: Pump technology terms NPSH value [m
- Page 12 and 13: Loss of head calculation Loss of he
- Page 14 and 15: Loss of head calculation Example: F
- Page 16 and 17: Centrifugal pumps Feat ures of t he
- Page 18 and 19: Centrifugal pumps Correction of the
- Page 20 and 21: Centrifugal pumps Pumps connected i
- Page 22 and 23: Centrifugal pumps Centrifugal pump
- Page 24 and 25: Centrifugal pumps Centrifugal pump
- Page 26 and 27: Centrifugal pumps Power consumption
- Page 28 and 29: Centrifugal pumps Self- priming cen
- Page 30 and 31: Centrifugal pumps Multistage centri
- Page 32 and 33: Positive displacement pumps Perform
- Page 34 and 35: Positive displacement pumps Selecti
- Page 36 and 37: Positive displacement pumps Case 1:
- Page 40 and 41: Positive displacement pumps Case 2:
- Page 42 and 43: Positive displacement pumps Case 2:
- Page 44 and 45: Positive displacement pumps Case 3:
- Page 46 and 47: Positive displacement pumps Rotary
- Page 48 and 49: Positive displacement pumps Case 1:
- Page 50 and 51: Positive displacement pumps Case 2:
- Page 52 and 53: Positive displacement pumps Case 2:
- Page 54 and 55: Positive displacement pumps Case 3:
- Page 56 and 57: Positive displacement pumps Case 3:
- Page 58 and 59: Mechanical seal selection Double me
- Page 60 and 61: Mechanical seal selection “Face t
- Page 62 and 63: Mechanical seal selection Elastomer
- Page 64 and 65: Pump cleaning SIP After CIP cleanin
- Page 66 and 67: Index Cavitation . . . . . . . . .
Example:<br />
Q = 3000 l/h<br />
H = 120 m ∪ p = 12 bar<br />
η = 10 mPa s<br />
Step 1:<br />
speed correction<br />
stated in the diagram: p = 3.8 bar.<br />
Def ine now t he speed required f or t he correct ed pressure.<br />
Positive<br />
displacement<br />
pumps<br />
Case 2:<br />
viscous product<br />
η up to 200 mPa s
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