To understand the pump or it’s working principle, there are few pump basics terms are required to know. These are.
# Volumetric flow rate - Volume flow rate means the capacity of the liquid per unit time which is transfer through the pumps.
- It is the rate of water flow.
- Pump capacity is expressed in volumetric flow rate and head.
- It is measure in m3/s or ft3/s.
- The volume of flow, ‘V’ and time is ‘t’, then the volume flow rate,
q = V/t
If the mass flow rate is ‘m’, and density is ‘ρ’, and the volume flow rate,
Then, we can write,
m = ρ x q,
or, q = m/ρ
Hence, it can be defined as the ratio of mass flow rate to density.
In S.I. units, the volumetric flow rate is measured in m/s, and F.P.S unit, it is measured in
ft/min.
# Shut-off head - The shut-off head is one of the most important parameters in the pump. It is defined as the head with respect to zero volumetric flow rate.
# Static Head - Static head means the height difference between the elevation of the source of liquid and the elevation of the discharge liquid.
- Suction static head is totally depending on the elevation.
- It doesn’t depend on the flow rate.
- It depends on the specific gravity of the liquid, at a given pressure.
# Static suction head (hs) - The static suction head is a part of the static head.
- It is used when liquid source is above the pump center line.
- It describes the height from the liquid source to the pump center.
- Normally it is denoted by ‘hs’.
- This value is considered as +ve.
- Doesn’t depend on the liquid flow rate.
- Depends on the specific gravity, at a given pressure.
# Suction lift - This term is used when pump is placed above the liquid surface, elevation wise.
- This is the vertical distance between the liquid surface and the pump center line, when pump is placed above.
- This height is limited to 10m, due to the limitation of atmosphere.
- This value is considered as, -ve, as it is always opposite direction to static suction head.
# Static discharge head (hd) - The static discharge head is also a part of the static head.
- It is used to specify the distance between the elevation of the liquid in the destination and - the pump center line.
- Normally it is denoted by ‘hd’.
- Doesn’t depend on the liquid flow rate.
- Depends on the specific gravity, at a given pressure.
# Friction head - The pump has a piping system and all pipes will have many fittings, bends, straight lengths based on the system design. Hence, these all provide the resistanceto the flow which is required to overcome so flow will be continuous in the system.
- This head is known as friction head & it is the loss that needs to be overcome.
- The friction head depends on the following,
* Size of the pipe
* Pipe condition
* Age of pipe
* Type of pipe
* Nos of fitting
* Nos. of bends
* Pipe length
* Total system configuration
* Liquid flow rate
* Type of liquid
# Total Head - The total head in a system is defined as the total pressure difference between the inlet and outlet of the pump.
- In case of source is above the pump, difference between the discharge head and the suction head plus the friction head.
- In case of source is below, it is the sum of discharge head, suction lift, and friction loss.
TDH = Static Height + Static Lift + Friction Loss
# Vapor pressure - at a given temperature, vapor pressure is the pressure that is exerted by the gas in equilibrium with either a solid or liquid in a closed container.
- It is the pressure, in which molecules enter the vapor state at a specified temperature. If you boil a liquid, you can observe it.
- It is simply an indication of the evaporation rate of the liquid.
- If the temperature increases, vapor pressure will also increase.
Various units are used for vapor pressure:
Pascals (Pa),
bar (bar),
tor (mm Hg),
atmospheres (atm),
# Net Positive Suction Head - The Net Positive Suction Head – NPSH – is defined as the difference between the Suction Head, and the Liquids Vapor Head and can be expressed as
NPSH = hs – hv,
Where,
Hs – Suction head
Hv – Liquid vapor head
There are two terms which are very important,
a] NPSHr
b] NPSHa
NPSHr
NPSHr means NPSH required for the pump selection. It is one of the main functions of the selection of pumps so that the pump will not have any cavitationproblems during operation.
- It is the lowest value of NPSH in which pump will run without any cavitation.
- It is normally provided by manufacturer.
Best wat way to determine it by actual testing.
NPSH-R is the value at which the discharge pressure is reduced by 3% because of the onset of cavitation.
NPSHa
NPSHa means NPSH available. It is calculated from the suction side of the pump.
- It is basically a function of the system based on which a pump operates.
There are two options.
Option-1
: NPSHa when the pump is below the source,
NPSHa = Pa + hs – pv – pf
Where,
Pa – Absolute pressure head on the liquid surface
Hs – static head above pumps center line
pv – absolute liquid vapor pressure head at pumping temperature
pf – the suction friction head losses.
Option-2
: NPSHa when the pump is above the source,
NPSHa = Pa – hs – pv- pf
NPSH-A is always more than NPSH-R for any operating conditions to avoid cavitation of pumps.
# Specific speed - Specific speed or pump specific speed is defined as the parameter to specify the size or shape of the pump impeller. It is a dimensionless parameter.
Specific speed means, the following,
- It helps to select appropriate impeller size.
- It depends on shaft speed.
- It also depends on the flow rate and differential head at BEP.
- It is essential when comparison between two pumps are required.
- It doesn’t depend on pump size.
The friction head depends on the following,
* Shaft speed
* Flow rate
* Differential head etc.
# Theoritical pumping power - Theoretical Pump power calculation, P
Here, P = ρ x g x q x h,
Where,