Pump Notes and Calculations Pumps
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Fluid Power Notes Pneumatics .....
Hydrostatics
The following notes should enable a mechanical engineer to establish basic flow conditions and head losses along pipe routes in which fluids are flowing. The equations are most relevant to liquids although approximate sizing for gases can be carried out if appropriate correction factors are used,where necessary, and low gas velocities are considered.
A = Pipe Cross Section Area (m^{2}) a = Velocity of sound ( m /s) c _{ p} = Specific Heat Capacity at Constant pressure (kJ/(kg K)) c _{ v} = Specific Heat Capacity at Constant Volume (kJ/(kg K)) ε = Pipe roughness (m) ε _{mm} = Pipe roughness (mm) D = diameter (m) f = friction factor f_{T} = friction factor (flow in zone of complete turbulence). h = Specific Enthalpy (kJ/kg ) k = Thermal Conductivity (W/(m K)) r = radius of pipe bend (m) K = f (L/D ) L = Pipe Length (m) 
p = Absolute Pressure N / m^{2} Pr = Prantl Number =c _{ p}. mu / k (Dimensionless) Q = Volume flow Rate (m^{3} /s ) q = Heat Input per unit mass ( kJ /kg ) R = Gas Constant = R _{o} / M (kJ /(kg.K) Re = Reynolds Number = v.ρD/μ t = Temperature (C ) T = Absolute Temperature (K) u = Specific Internal Energy (kJ/kg) v =Fluid Velocity (m/s) w = Work Output per unit mass (kJ/kg) ρ = Density ( kg /m^{3} ) μ =Fluid Viscosity = (Ns/m^{2} = Pa s) z = Elevation (m ) g = gravitational acceleration ( 9.81 m /s^{2}) 
Fluid flowing in pipes has two primary flow patterns. It can be either laminar when all of the fluid particles flow in parallel lines at even velocities and it can be turbulent when the fluid particles have a random motion interposed on an average flow in the general direction of flow. There is also a critical zone when the flow can be either laminar or turbulent or a mixture. It has been proved experimentally by Osborne Reynolds that the nature of flow depends on the mean flow velocity (v), the pipe diameter (D), the density (ρ) and the fluid viscosity Fluid Viscosity( μ). A dimensionless variable for the called the Reynolds number which is simply a ratio of the fluid dynamic forces and the fluid viscous forces , is used to determine what flow pattern will occur. The equation for the Reynold Number is
For normal engineering calculations , the flow in pipes is considered laminar if the
relevant Reynolds number is less than 2000, and it is turbulent if the Reynolds number is greater than
4000. Between these two values there is the critical zone in which the flow can be either laminar or turbulent
or the flow can change between the patterns...
It is important to know the type of flow in the pipe when assessing friction losses
when determining the relevant friction factors
Reference :
The steady flow equation steady flow equation (energy per unit mass ) for a system is identified below...
Reference... Steady Flow
If q = w = 0 and the fluid is incompressible and frictionless
and if the variables are converted to measured heads of the fluid , that is the units are per
unit weight (ρg)  then the Bernoulli's equation results ..
Reference .. Bernoulli's Equation ideal fluids
..
In real flow systems there are losses due to internal and wall friction which result in increase in the internal energy of the fluid. (q > 0). Reference Bernoulli's Equation real Fluids . The bernoulli equation is modified to reflect these losses by adding a term h _{f} = Head loss due to friction.= (u_{2} u_{1}  q) The modified bernoullis equation is therefore ..
The object of most pipe flow head loss calculations is to determine the friction head loss and allow estimation of the pump /compressor power required to pump the fluid along the piping. In most fluid transfer cases the fluid is a incompressible (a liquid) and the flow rate (Q) is constant along the pipe run and therefore the velocity at any point can easily be calculated. The head (z) can also be easily obtained from the pipeline geometry. The system pressure and head loss are therefore the variables generally subject to the detailed pipeline calculations....
In determining the head loss (pressure drop) along a pipe as
a result of friction losses it is first necessary to determine the following:
Diameter (m), Length (m), Fluid Viscosity( μ),
Fluid density (ρ) and the fluid velocity (v). It is then necessary to obtain the
relevant Reynolds number..
The equation for the Reynold Number
Consistent units to be used i.e Typically ρ = kg/m^{3},
v = m/s, D= m, μ = Ns/m^{2}
( 1 Ns/m^{2} = 10^{3}cP)
The value for the Reynold number is to be used to evaluate if
the flow is laminar or turbulent and can be used to obtain the friction factor " f "
from a moody chart. The moody chart plots the friction factor (f) against the Reynold number
with a number of different plotted lines for different values of absolute roughness/Diameter .
The head loss along the pipe can now be calculated using the DarcyWeisbach equation
The result of the calculation is in units of head of the fluid. . It is based on the pipe being all one dia and the fluid is incompressible
For a single pipe line with a number of fittings the total head loss is calculated as
K _{p} = f (L/D) for the length of pipe. ( this may be made up of ∑ f(L/D). for a number of different pipe lengths of different diameters )
K _{1..n} = f_{T}(L/D) equivalent for each fitting
A Moody chart (see below) is used to determine the turbulent flow friction factor from the Reynolds number and
the relative roughness of the pipe. If the flow is laminar then the fricton factor is 64/Re.
Note: it is suggested that for laminar flow in pipe at Re number approaching 2000 the above K values are used for bends and fitting with reasonable accuracy
A moody chart and tables for roughness values and (L/D) factors for various fittings are provided below
Note:
In the moody chart above (ε; /D ) is identified with both
numerator and denominator in metres (for consistency with all other equations on this page.
It is probably more convenient to express both in (mm).i.e a 50mm cast iron pipe
(ε _{mm}; /D_{mm} ) would simply be (0,203 /50 ).
Type of Pipe  ε; .10^{3}..( = ε;_{mm} ) 
Cast Iron  0,203 
Galvanised Steel  0,152 
Steel/Wrought Iron  0,051 
Rivetted Steel  0,91  9,1 
Asphalted Cast Iron  0,12 
WoodStave  0,18  0,91 
Concrete  3,0 
Spun Concrete  0,203 
Drawn Copper, Brass Steel,Glass  Smooth 
The losses through fittings are generally evaluated by obtaining K = f_{T}(L/D)
Table of pipe friction values for clean pipe in region of complete turbulence
Nominal size(mm)  15  20  25  32  40  50  65,80  100  125  150  200,250  300,400  450,600 
f_{T}  0,027  0,025  0,023  0,022  0,021  0,019  0,018  0,017  0,016  0,015  0,014  0,013  0,012 


The K_{180} value for a 180^{o} bend may be derived from the equivalent K_{90} which is calculated from the above tables using the equation
The K_{180} = 0,25.π.f_{T} . r/D + 1,5.K_{90}
For laminar fluids with low Re numbers ( "<" 500) the K values obtained using the above are probably very innaccurate. The table below illustrates how this affects the K values
Fitting  K values for low Reynolds Number fluids  
Re = 1000  500  100  50  
90 deg Elbow Short Radius  0,9  1  7,5  16 
Gate Valve  1,2  1,7  9,9  24 
Globe Valve  11  12  20  30 
Plug Valve  12  14  19  27 
Angle Valve  8  8.5  11  19 
Swing check Valve  4  4,5  17  55 
The losses through these fitting are generally evaluated by
first obtaining β = d_{2} / d_{1}
Important Note: the resulting K values as tabled below are based on the flow velocity in the larger
pipe if the flow velocity in the small pipe is used to evaluate the head loss then the K values tabled below should
be multiplied by ( β ) ^{4} = (d_{2} / d_{1}) ^{4}
β  K _{e}  K _{c}  K _{o}  β  K _{e}  K _{c}  K _{o}  
0.15  1887.42  965.43  2852.85  0.6  3.16  2.47  5.63  
0.2  576  300  876  0.65  1.87  1.62  3.49  
0.25  225  120  345  0.7  1.08  1.06  2.14  
0.3  102.23  56.17  158.4  0.75  0.6  0.69  1.29  
0.35  51.31  29.24  80.55  0.8  0.32  0.44  0.76  
0.4  27.56  16.41  43.97  0.85  0.15  0.27  0.42  
0.45  15.51  9.72  25.23  0.9  0.06  0.14  0.2  
0.5  9  6  15  0.95  0.01  0.06  0.07  
0.55  5.32  3.81  9.13  1  0  0  0 
Medium  Pressure (bar)  Service  Velocity (m/s)  Notes 
Steam (sat)  0  1.7  Heating  20 to 30  + 100mm dia 
Steam (sat)  over 1.7  Process  30 to 50  +150mm dia 
Steam (sup)  over 14  Process  30 to 100  +150mm dia 
Air  Forced Air Flow  5 to 8  e.g. AC Reheat  
Water    General  1 to 3  
Water  Concrete Pipe  4,7  
Water  Pump Suction  1,2  
Water  Horizontal Sewer  0,75  Minimum  
Water  Pump discharge  1,2 to 2,5  Minimum  
Water  Boiler Feed  2,4 to 4,6  Minimum  
Oil  Hydraulic Systems  2,1 to 4,6  Minimum  
Ammonia  Compressor Suction  25  Max. Permissable  
Ammonia  Compressor Discharge  30  Max. Permissible 