Momentra

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    • q
      Volume flow rate
    • g
      Local acceleration due to gravity
    • 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
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