Operation



Eductors for Liquids, Solids, Slurries & Liquid Jet Gas Eductors




 
Eductor for Liquids, Slurries, Solids, Liquid Jet Gas Eductor
Eductor - Principle of Operation
 

  • A high pressure liquid enters the specially designed nozzle  which increases the fluid velocity and causes the motive pressure (P1) to be  dropped to equal  the suction pressure (P2). 
  • This pressure drop allows the suction fluid to enter the eductor body and mixes with the motive fluid in the throat section.
  • The diffusers section reduces the fluid back to pipeline velocities which allows recovery of some of the fluid pressure (P3). 
  • The performance of the eductor is determined by the motive & suction flow rates, pressure differential between the motive, suction and discharge ports, fluid temperature and the precise internal eductor geometry.





Steam Ejectors, Gas Ejectors, Air Ejectors, Vacuum Ejectors & Thermocompressors




 
Ejectors, Gas Ejectors, Steam Ejectors, Air Ejectors, Vacuum Ejectors, Thermocompressors
Ejector Principle of Operation
 

  • Ejectors differ from eductors in that they operate with gaseous fluids, steam or air for example, instead of liquids. They are primarily designed to operate at sonic conditions and operate on the two sonic choke principle. 
  • Ejectors can be designed to operate at Sub Critical velocities in certain circumstances
  • Motive gas is passed through the nozzle and accelerated to critical velocities (V1) to create a sonic choke. The kinetic energy from the motive velocity and pressure drop generates the suction and draws in the secondary, suction, gas. 
  • The throat diameter creates a second sonic choke (V2) which limits the suction flow rate and is used to determines the achievable counter / discharge pressure.





Mixing Eductors, Tank Mixers & Sparger Nozzles



 
Mixing Eductor, In Tank Eductor, Tank Agitator, Fluid Mixer
Mixing Eductor Principle of Operation
 

  • A mixing eductor works on the same principle as a standard eductor and can be used for any liquid or liquid slurry with a viscosity of less than 100cP and 2 SG.
  • Operationally however they differ in that the mixing eductor is installed in a tank rather than in a pipeline with open suction and discharge ports.
  • Requires a minimum of  2 bar pressure differential between motive fluid and the tank head pressure (level of fluid in the tank).
  • Suction flowrate (Fs) is fixed at 3 times the motive flowrate (FM) 
  • Discharge plume of 1 metre length per 0.2 bar motive to suction differential pressure possible.




Instantaneous / Inline Steam Heaters



 
Instantaneous Heater, Steam Heater, Inline Heater, Inline Steam Heater
Heater Principles of Operation
 

  • The instantaneous heater is a device used for heating newtonian fluids with low pressure steam. 
  • There are two types of heater design dependent on the pressures involved. 
            A type - Steam pressure < water pressure
            B type - Steam pressure > water pressure

  • Both designs work on the same principle of equalising the steam/water pressures to allow the two to mix via impulse energy transfer.
  • The number of holes in the mixing nozzle controls the heating by dictating the amount of steam which is allowed to enter.
  • Heaters have a fixed designed therefore are suitable for a relatively stable operating duty only. However multiple heaters can be used together.  

Spray type Desuperheaters



 
Desuperheater, Spray Type Desuperheater, Spool Type Desuperheater
Desuperheater Principles of Operation
 

  • The spray type desuperheater is used to reduce the temperature of steam to near saturation temperatures (+ 3 degC) from superheated temperatures.
  • Cooling is achieved by evaporation of a cooling medium upon contact with the steam flow.
  • The cooling medium is sprayed into the steam flow in the form of fine droplets to increase fluid surface area and therefore fluid / steam interaction.
  • The cooling fluid must be at a pressure of at least 1 bar greater than the superheated steam flow.
  • Dependent on the required reduction in superheated steam temperature pressure drops across the desuperheater range from 0.1 to 1 bar.
  • Having a fixed geometry spray type desuperheaters are designed for a relatively stable range of operation. Having a maximum turn down of 2:1.