A pump or compressor is a physical contrivance that is used to deliver fluids from one location to another through conduits
Pump
Used when the fluid is a liquid
Compressor
Used when the fluid is a gas
Basic requirements to define the application
Suction and delivery pressures
Pressure loss in transmission
Flow rate
Special requirements may exist in food, pharmaceutical, nuclear, and other industries that impose material selection requirements of the pump
Primary means of transfer of energy to the fluid that causes flow
Gravity
Displacement
Centrifugal force
Electromagnetic force
Transfer of momentum
Mechanical impulse
Combination of these energy-transfer mechanisms
Displacement and centrifugal force are the most common energy-transfer mechanisms in use
Pumps and compressors are designed per technical specifications and standards developed over years of operating and maintenance experience
Standards governing pumps and compressors
ASME Standards
API Standards
Hydraulic Institute Standards
NFPA Standards
Major types of pumps
Positive displacement
Dynamic (kinetic)
Lift
Electromagnetic
Piston pumps are positive displacement pumps
The most common centrifugal pumps are of dynamic type
Ancient bucket-type pumps are lift pumps
Electromagnetic pumps use electromagnetic force and are common in modern reactors
Canned pumps are also becoming popular in the petrochemical industry because of the drive to minimize fugitive emissions
Displacement
Discharge of a fluid from a vessel by partially or completely displacing its internal volume with a second fluid or by mechanical means
Displacement-type fluid-transport devices
Adaptable to high-pressure operation
Flow rate through the pump is variable
Mechanical considerations limit maximum throughputs
Capable of efficient performance at extremely low-volume throughput rates
Centrifugal force
Applied by means of the centrifugal pump or compressor
Centrifugal fluid-transport devices
Discharge is relatively free of pulsation
Mechanical design lends itself to high throughputs, capacity limitations are rarely a problem
Capable of efficient performance over a wide range of pressures and capacities even at constant-speed operation
Discharge pressure is a function of fluid density
Relatively small high-speed devices and less costly
Axial-flow compressor or pump
Combines the use of centrifugal force with mechanical impulse to produce an increase in pressure
Electromagnetic force
Used when the fluid is an electrical conductor, as is the case with molten metals, to impress an electromagnetic field around the fluid conduit in such a way that a driving force that will cause flow is created
Transfer of momentum
Deceleration of one fluid (motivating fluid) in order to transfer its momentum to a second fluid (pumped fluid)
Jets and eductors
Absence of moving parts and simplicity of construction
Relatively inefficient devices
When air or steam is the motivating fluid, operating costs may be several times the cost of alternative types of fluid-transport equipment
Environmental considerations in today's chemical plants often inhibit their use
Mechanical impulse
Usually combined with one of the other means of imparting motion, as in the case of axial-flow compressors and pumps, and the turbine or regenerative-type pump
Capacity
The mass rate of fluid flow through a fluid-transport device
Head
The total pressure differential measured immediately before and after the fluid-transport device, usually expressed in the height of column of fluid equivalent under adiabatic conditions
Capacity (SI units)
Cubic meters per hour (m³/h) for both liquids and gases
Capacity (U.S. customary units)
U.S. gallons per minute (gal/min) for liquids and in cubic feet per minute (ft³/min) for gases
When gases are being handled, capacity must be related to a pressure and a temperature, usually the conditions prevailing
Measurement of Performance
The product of (1) the mass rate of fluid flow through a fluid-transport device and (2) the total pressure differential measured immediately before and after the device, usually expressed in the height of column of fluid equivalent under adiabatic conditions
Head
The total pressure differential measured immediately before and after a fluid-transport device, usually expressed in the height of column of fluid equivalent under adiabatic conditions
Capacity is expressed in cubic meters per hour (m³/h) for both liquids and gases in SI units, and in U.S. gallons per minute (gal/min) for liquids and in cubic feet per minute (ft³/min) for gases in U.S. customary units
Density or specific gravity must be used for conversion to mass rate of flow when using volume units for capacity
For gases, capacity must be related to a pressure and a temperature, usually the conditions prevailing at the machine inlet
All heads and other terms are expressed in height of column of liquid
Total Dynamic Head (H)
The total discharge head (hd) minus the total suction head (hs)
Total Suction Head (hs)
The reading of a gauge at the suction flange of a pump (corrected to the pump centerline), plus the barometer reading and the velocity head (hes) at the point of gauge attachment
If the gauge pressure at the suction flange is less than atmospheric, the reading of a vacuum gauge is used for hgs with a negative sign