Figures and Tables for Fluid Flow
No. |
Description |
No. |
Author |
4.1 |
Properties of Water. |
||
4.2 |
Physical Properties of Air at 1 atm. |
||
4.3 |
Kinematic Viscosity of fluids. |
Fig A-2 |
Crane |
4.4 |
Flow Coefficient C for Nozzles. |
Fig A-20 |
Crane |
4.4 |
Flow Coefficient C for square-edged Orifices. |
Fig A-20 |
Crane |
4.5 |
Net Expansion Factor Y for Compressible Flow Through Nozzles and Orifices. |
Fig A-20 |
Crane |
4.6 |
Critical Pressure Ratio, rc for Compressible Flow through Nozzles and Venturi Tubes. |
Fig A-21 |
Crane |
4.7 |
Resistance in Pipe due to Sudden Enlargement and Contraction. |
Fig A-26 |
Crane |
4.8 |
Resistance due to Pipe Entrance and Exit. |
Fig A-26 |
Crane |
4.9 |
Additional Frictional Loss for Turbulent Flow Through Fittings and Valves. |
Table 5.14 |
Perry |
4.10 |
Equivalent Length of Pipe Fittings and Valves. |
Perry |
|
4.11 |
Properties of Steel Pipe. |
Table 6.6 |
Perry |
4.11 |
Roughness factors (expressed in feet) for Commercial Pipes. |
Fig A-4 |
Crane |
4.12 |
Friction factor Chart. |
Fig 5-10 |
McCabe & Smith |
4.13 |
Friction factor Chart, NRe Öf vs. f. |
Fig 5-11 |
McCabe & Smith |
4.14 |
Upper Limits of Specific Speeds of Single-Stage Single- and Double-suction Centrifugal Pumps handling clear water at 85 F (Perry, Fig 6-10). |
Perry |
|
4.15 |
Upper Limits of Specific Speeds of Single-Suction Mixed-Flow and Axial-Flow Pumps (Perry, Fig 6-11). |
Perry |
|
4.16 |
Approximate Relative Impeller Shapes and Efficiency Variations of Various Specific Speeds of Centrifugal Pumps (Perry, Fig 6-12). |
Perry |
|
4.17 |
Typical Pump Suction and Discharge Piping Arrangements (Perry, Fig 6-13) |
Perry |
|
4.18 |
Typical Selection Chart for Centrifugal Pumps (Perry, Fig 6-16) |
Fig 6-16 |
Perry |
Crane
McCabe & Smith, Unit Operations in Chemical Engineering
Perry, Chemical Engineers' Handbook, 6th Edition