Page 1 of 20 Objectives - To calculate the System Differential Pressure - To determine the Net Positive Suction Head Avaliable in the - To determine the required Brake Horsepower - To select a suitable Motor Horse Power rating for the Pump Basics - Diesel Transfer Pumps are positive displacement pumps - Specific gravity of Diesel is 0.84 - 0.89; Used value is 0. - - Hydraulic Diameter = 0.0508 m (2 in) - Suction Pipe length is 1 m. - Discharge pipe length is 4.27 m - Discharge Vessel Elevation head is 4 m - Specific roughness of pipe material is 0.00004572 m References 1. API 676: Positive Displacement Pumps, Rotary 2. CRANE: Flow of Fluids Through Valves, Fittings and Pipe Acceleration due to gravity is 9.81 m/s 2
This document is posted to help you gain knowledge. Please leave a comment to let me know what you think about it! Share it to your friends and learn new things together.
Transcript
Page 1 of 10
Objectives
- To calculate the System Differential Pressure- To determine the Net Positive Suction Head Avaliable in the system- To determine the required Brake Horsepower- To select a suitable Motor Horse Power rating for the Pump
Basics
- Diesel Transfer Pumps are positive displacement pumps- Specific gravity of Diesel is 0.84 - 0.89; Used value is 0.85
- - Hydraulic Diameter = 0.0508 m (2 in)- Suction Pipe length is 1 m.- Discharge pipe length is 4.27 m- Discharge Vessel Elevation head is 4 m- Specific roughness of pipe material is 0.00004572 m
References
1. API 676: Positive Displacement Pumps, Rotary2. CRANE: Flow of Fluids Through Valves, Fittings and Pipe
Acceleration due to gravity is 9.81 m/s2
2 of 10
DEFINITION OF TERMS
∆P - Differential Pressure
BHP - Brake Horsepower
D - Hydraulic Diameter
f - Darcy Friction factor
g - Gravitational Acceleration
- Head losses due to friction
- Pressure head in vessel
HHP - Hydraulic Horse Power
- Vapour Pressure Head
K - Resistance Coefficients for pipe fittings
l - Straight pipe length
NPSHa - Net Positive Suction Head Available
OD - Outside Diameter of Pipe
P - Pressure in Vessel
Q - Flow Rate
Re - Reynold's Number
SG - Specific Gravity
V - Velocity
Z - Elevation Head
ε - Absolute Roughness
ѵ - Kinematic Viscosity
hf
hp
hvp
3 of 10
4 of 10
SUCTION SIDE
Flow Rate (Q) = 0.05560
Specific Gravity = 1
Hydraulic Diameter (D) = 0.15 m
Suction Head Calculation
Parameters
Suction Vessel Pressure (P) = 1.0135 bar (Atm)
= 8.01000E-07
= 0.00004572 m
Pipe Length (L) = 1 m (below pump suction)
= 10.331 m
Elevation Head = 1 m
Friction Head
Head Loss in Pipe length (m)
Average Velocity - V = 3.146316386
Reynolds Number, Re = 589197.8251
Darcy Friction Factor,f = 0.016237308
Head loss in pipe length (m) = 0.055 m
Head loss in fittings (m)
0 Reducers K = 5
0 Ball Valves K = 0
0 Elbows K = 0
1 Entrance K = 0.78
Total K for fittings = 5.78
Total Head loss in fittings = 0.047 m
Friction Head = 0.102 m
Total Suction Head = 11.229 m
(All formulas used in the calculations above are shown in Appendix 1)
m3/s
Suction vessel pressure head (hp) + Elevation head (Z) - Friction Head (hf)
Kinematic Viscosity (ν) m2/s
Specific Roughness (Є)
Suction Vessel Pressure Head (hp)
m/s2
1 90Oelbow, 1 45O deg elbow)
5 of 10
6 of 10
DISCHARGE SIDE
Flow Rate (Q) = 0.05560
Specific Gravity = 1
Hydraulic Diameter (D) = 0.15 m
Discharge Head Calculation
Parameters
Discharge Vessel Pressure (P) = 1.0135 bar (Atm)
= 8.01E-07
= 0.00004572
Pipe Length (L) = 200 m
Discharge Vessel Pressure Head = 10.331 m
Elevation Head = 200 m
Friction Head
Head Loss in Pipe length (m)
Average Velocity - V = 3.146316
Reynolds Number = 589197.8
Darcy Friction Factor = 0.016237
Head loss in pipe length (m) = 10.923 m
Head loss in fittings (m)
3 Elbows K = 1.721155
1 Exit K = 0.016237
0 Check Valve K = 0
1 Ball Valve K = 0.048712
Total K for fittings = 1.786104
Total Head loss in fittings = 0.015 m
Friction Head = 10.938 m
Total Discharge Head = 221.269 m
m3/s
Discharge vessel pressure head (hp) + Elevation head (Z) + Friction Head (hf)
Kinematic Viscosity (ν) m2/s
Specific Roughness (ε)
m/s2
7 of 10
(All formulas used in the calculations above are shown in Appendix 1)
8 of 10
PERFORMANCE REQUIREMENTS
Total Dynamic Head = Total Discharge Head - Total Suction Head
= 210.040 m
Pressure Differential = 20.6 bar
Hydrualic Horse Power (HHP) = 11453.6 kW 50.30000 hp
Pump Efficiency = 75 %
Brake Horse Power = 15271.47 67.06667 hp
Rated Horse power = 17562.19 77.12667 hp
Rated Motor Nameplate HP
Net Positive Suction Head Available (NPSHa)
Vapour pressure of liquid = 0.6 bar
Vapour pressure head of liquid = 6.116 m
NPSHa = 5.11 m
(All formulas used in the calculations above are shown in Appendix 1)
Suction vessel pressure head (hp) + Elevation head (Z)