Centrifugal Pumps Design and Application 2nd ed - Val S. Lobanoff, Robert R. Ross (Butterworth-Heinemann, 1992)
7 Double-Suction Pumps and Side-Suction Design The double-suction single-stage pump is, perhaps, the most widely used pump throughout the industrial world. Applications range from light duty building trade pumps to heavy duty pipeline injection pumps (Figure 7-1). The double-suction is a very simple machine whose initial cost is relatively low. Above 700-1,000 GPM, efficiency is high and required NPSH is low. All modern double-suction pumps are designed with double-volute casing to maintain hydraulic radial balance over the full range of the head-capacity curve. Having a double-suction impeller, the pumps are theoretically in axial balance. Double-suction pumps often have to operate under suction lift, run wide open in a system without a discharge valve, or satisfy a variable capacity requirement. These pumps may be quite large, pump high capacities, and handle pumpage with gas or entrained air. In spite of all this, they are expected to operate without noise or cavitation. Suction passage design should therefore be based on the best available technical "know-how," and liberties should not be taken during the design process. Pump Casing Double-Suction Pump Design The double-suction, double-volute casing is designed in identical manner to the single-suction pump, as described in Chapter 5. The specific speed, N s , of a double-suction pump is identical to the single-suction unit. Do not divide calculated pump specific speed by the square root of 77
Figyre 7-1. Inc. of Byron Jackson/United Pumps),
- Page 42 and 43: Specific Speed and Modeling Laws 27
- Page 44 and 45: Impeller Design 29 Figure 3-1. Requ
- Page 46 and 47: Impeller Design 31 Figure 3-4. Capa
- Page 48 and 49: Impeller Design 33 Step 8: Estimate
- Page 50 and 51: Impeller Design 35 Figure 3-7. Volu
- Page 52 and 53: impeller Design 37 (2) 5 , as final
- Page 54 and 55: Impeller Design 39 The vane develop
- Page 56 and 57: Impeller Design 41 Figure 3-12. Are
- Page 58 and 59: impeller Design 43 Figure 3-16. Inf
- Page 60 and 61: 4 General Pump Design It is not a d
- Page 62 and 63: General Pump Design 4? Figure 4-1.
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- Page 66 and 67: Volute Design 51 Figure 5-1. Volute
- Page 68 and 69: Volute Design 53 Figure 5-2. Radial
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- Page 72 and 73: Volute Design 57 Figure 5-4. Effici
- Page 74 and 75: Volute Design 59 Figure 5-5. Typica
- Page 76 and 77: Volute Design 61 Figure 5-8. Univer
- Page 78 and 79: Volute Design S3 Manufacturing Cons
- Page 80 and 81: 6 Design of Multi-Stage Casing Mult
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- Page 88 and 89: Design of Multi-Stage Casing 73 sec
- Page 90 and 91: Design of Multi-Stage Casing 75 Fig
- Page 94 and 95: Double-Suction Pumps 79 two. Experi
- Page 96 and 97: Double-Suction Pumps 81 Figure 7-3.
- Page 98 and 99: Double-Suction Pumps 83 LOCATION AR
- Page 100 and 101: 8 NPSH The expressions NPSHR and NP
- Page 102 and 103: NPSH 87 Predicting NPSHR The other
- Page 104 and 105: NPSH 89 Figure 8-4. Pressure loss b
- Page 106 and 107: NPSH 91 SUCTION VELOCITY TRIANGLES
- Page 108 and 109: NPSH 93 Figure 8-8. Performance cur
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- Page 112 and 113: NPSH 97 Figure 8-13. Plate inserts
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- Page 116 and 117: NPSH 101 Figure 8-19. Estimating K
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- Page 126 and 127: Part 2 Application
- Page 128 and 129: 9 by Erik B. Fiske BW/JP Internatio
- Page 130 and 131: Vertical Pumps 115 Figure 9-2. Well
- Page 132 and 133: Vertical Pumps 117 Figure 9-4. Subm
- Page 134 and 135: Vertical Pumps 119 Figure 9-6. Inst
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7<br />
Double-Suction<br />
<strong>Pumps</strong> <strong>and</strong><br />
Side-Suction<br />
<strong>Design</strong><br />
The double-suction single-stage pump is, perhaps, the most widely<br />
us<strong>ed</strong> pump throughout the industrial world. <strong>Application</strong>s range from<br />
light duty building trade pumps to heavy duty pipeline injection pumps<br />
(Figure 7-1).<br />
The double-suction is a very simple machine whose initial cost is relatively<br />
low. Above 700-1,000 GPM, efficiency is high <strong>and</strong> requir<strong>ed</strong><br />
NPSH is low. All modern double-suction pumps are design<strong>ed</strong> with double-volute<br />
casing to maintain hydraulic radial balance over the full range<br />
of the head-capacity curve. Having a double-suction impeller, the pumps<br />
are theoretically in axial balance. Double-suction pumps often have to<br />
operate under suction lift, run wide open in a system without a discharge<br />
valve, or satisfy a variable capacity requirement. These pumps may be<br />
quite large, pump high capacities, <strong>and</strong> h<strong>and</strong>le pumpage with gas or entrain<strong>ed</strong><br />
air. In spite of all this, they are expect<strong>ed</strong> to operate without noise<br />
or cavitation. Suction passage design should therefore be bas<strong>ed</strong> on the<br />
best available technical "know-how," <strong>and</strong> liberties should not be taken<br />
during the design process.<br />
Pump Casing<br />
Double-Suction Pump <strong>Design</strong><br />
The double-suction, double-volute casing is design<strong>ed</strong> in identical manner<br />
to the single-suction pump, as describ<strong>ed</strong> in Chapter 5. The specific<br />
spe<strong>ed</strong>, N s , of a double-suction pump is identical to the single-suction<br />
unit. Do not divide calculat<strong>ed</strong> pump specific spe<strong>ed</strong> by the square root of<br />
77