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Prepared by,
Asst. prof. Krishna parmar
Environmental Engineering
Diwaliba Polytechnic, Mahuva
Venturi scrubber
Contents:
 Introduction
 Principle of Operation
 Diagram
 Particle Collection
 Gas collection
 Operating characteristics of ejector venturi
 Advantage
 Disadvantage
 Maintenance problem
Introduction:
 An industrial particulate and Gas
collection device.
 Installed on the exhaust flue gas stacks of large
furnaces.
 A single nozzle is used instead of many nozzles
 Operates at higher pressure and higher injection
rates
Principle of operation:
 Scrubbing liquid is supplied to the motive inlet under
pressure.
 As a result of the large drop in liquid pressure across
the nozzle, a high velocity liquid spray exits the
nozzle.
 This atomized liquid provides surface area for
transfer of mass from the gas to the liquid phase and
allows for capture of particulates from the gas phase
due to impaction.
 In addition, the velocity of the liquid spray creates a
negative pressure which pulls gas into the Scrubber.
Particle collection:
 larger than 1.0 µm in diameter
 Particle collection efficiency increases with
 an increase in nozzle pressure
 an increase in the liquid-to-gas ratio
 Increases in in pressure drop
Gas collection:
 Short gas-liquid contact time
 exhaust gas velocities very high
 removal efficiencies of 95% can be achieved
 Effective if the gas is very soluble or if a very reactive
scrubbing reagent is used
Operating characteristics of ejector venturi:
Pollutant Gases Particles
Pressure drop
(Δp)
1.3–13 cm of water 0.5-5 in of water
Liquid-to-gas ratio
(L/G)
7-13 l/m3 50-100 gal/1,000 ft3
Liquid-inlet pressure
(pL)
100-830 kPa 50-100 gal/1,000 ft3
Removal efficiency 95% for very soluble gases 1 µm diameter
Applications Pulp and paper industry
Chemical process industry
Food industry
Metals processing industry
Maintenance problems:
 Abrasion problems in the high-velocity areas -
nozzle and throat
 Constructed of wear-resistant materials because of
the high liquid injection rates and nozzle pressures.
 Maintaining the pump that recirculates liquid
Advantage:
 Low initial cost
 Small spatial requirement
 A fan is not required to move the gas
 Simultaneous removal of gases and particulates
 No moving parts
Disadvantage:
 Large pressure drop
 Sign of erosion when scrubbing abrasive medium
Venturi scrubber

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Venturi scrubber

  • 1. Prepared by, Asst. prof. Krishna parmar Environmental Engineering Diwaliba Polytechnic, Mahuva Venturi scrubber
  • 2. Contents:  Introduction  Principle of Operation  Diagram  Particle Collection  Gas collection  Operating characteristics of ejector venturi  Advantage  Disadvantage  Maintenance problem
  • 3. Introduction:  An industrial particulate and Gas collection device.  Installed on the exhaust flue gas stacks of large furnaces.  A single nozzle is used instead of many nozzles  Operates at higher pressure and higher injection rates
  • 4. Principle of operation:  Scrubbing liquid is supplied to the motive inlet under pressure.  As a result of the large drop in liquid pressure across the nozzle, a high velocity liquid spray exits the nozzle.  This atomized liquid provides surface area for transfer of mass from the gas to the liquid phase and allows for capture of particulates from the gas phase due to impaction.  In addition, the velocity of the liquid spray creates a negative pressure which pulls gas into the Scrubber.
  • 5.
  • 6. Particle collection:  larger than 1.0 µm in diameter  Particle collection efficiency increases with  an increase in nozzle pressure  an increase in the liquid-to-gas ratio  Increases in in pressure drop
  • 7. Gas collection:  Short gas-liquid contact time  exhaust gas velocities very high  removal efficiencies of 95% can be achieved  Effective if the gas is very soluble or if a very reactive scrubbing reagent is used
  • 8. Operating characteristics of ejector venturi: Pollutant Gases Particles Pressure drop (Δp) 1.3–13 cm of water 0.5-5 in of water Liquid-to-gas ratio (L/G) 7-13 l/m3 50-100 gal/1,000 ft3 Liquid-inlet pressure (pL) 100-830 kPa 50-100 gal/1,000 ft3 Removal efficiency 95% for very soluble gases 1 µm diameter Applications Pulp and paper industry Chemical process industry Food industry Metals processing industry
  • 9. Maintenance problems:  Abrasion problems in the high-velocity areas - nozzle and throat  Constructed of wear-resistant materials because of the high liquid injection rates and nozzle pressures.  Maintaining the pump that recirculates liquid
  • 10. Advantage:  Low initial cost  Small spatial requirement  A fan is not required to move the gas  Simultaneous removal of gases and particulates  No moving parts
  • 11. Disadvantage:  Large pressure drop  Sign of erosion when scrubbing abrasive medium