FK 40 - Tri-Canada
FK 40 - Tri-Canada FK 40 - Tri-Canada
Positive displacement pumps Case 2: viscous product η up to 500 mPa s Flow rate Q = 2000 l/h Tot al head H = 60 m Viscosit y η = 10 mPa s Step 1: define correction for the speed H = 60 m ∪ 6 bar read speed at H = 33 m (equal to p = 3.3 bar)
Step 2: read speed at H = 33 m (∪ 3.3 bar) read: speed n = 300 1/min Positive displacement pumps Case 2: viscous product η up to 500 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 38 and 39: 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 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 . . . . . . . . .
Positive<br />
displacement<br />
pumps<br />
Case 2:<br />
viscous product<br />
η up to 500 mPa s<br />
Flow rate Q = 2000 l/h<br />
Tot al head H = 60 m<br />
Viscosit y η = 10 mPa s<br />
Step 1:<br />
define correction for the speed<br />
H = 60 m ∪ 6 bar<br />
read speed at H = 33 m (equal to p = 3.3 bar)
Change language