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Problem C1: Spray
      Drying
    Katipunan, Hazel E.
    Lizardo, Syreanne C.
     Maniego, Carlo P.
      Revalo, Orly M.
          5ChE-A
• Objectives


   To calculate the heat effects involved in the
    operation of a spray dryer

   To determine the efficiency of the spray dryer
    used in terms of percentage recovery of the
    dried solids.
•Equipment / Materials
 Spray Dryer with Atomizer 220 V

 Air Compressor

 Anemometer

 Cotton

 Detergent
•Equipment / Materials

 Stirring Rod

 Collecting Jar

 500-mL beaker

 Distilled Water

 Timer
•Theory
Spray Dryer
•Theory
Spray Dryer
• Liquid feed is pumped into a spray-disk
  atomizer.

• Droplets   are formed inside cylindrical drying
 chamber.

• Cooledgas is drawn by an exhaust fan through
 a horizontal discharge line set in the side of
 chamber.
•Theory
Spray Dryer
• Exhaust air passes through cyclone separator.

• Dry solids settles out of the gas into the bottom
  of the chamber.
•Theory
Advantages of Spray Dryer:

• Very   short drying time

• Production   of hollow spherical particles

• Desired consistency, bulk density, appearance,
 and flow properties of products may obtained
 easily compared to other dryers
•Theory

• Yieldingfrom a slurry, in a single step, dry
 product is ready for package

• May   combine the functions of evaporator,
 classifier, dryer, crystallizer, or size reduction
 unit.
•Theory
Disadvantages of Spray Dryer:
• It is bulky and large equipment.



• It   is not always easy to operate.

• Bulk
     density of dry solid is often difficult to kept
 constant.
•Theory

Wet Bulb Temperature

• Is  the steady-state, non- equilibrium
 temperature reached by a small mass of liquid
 exposed under adiabatic conditions to a
 continuous stream of gas
•Theory
Method of      measuring   the   wet   bulb
temperature:

•A  thermometer or other temperature-
measuring device is covered by a wet wick,
which is saturated with pure liquid and
immersed in a stream of gas having definite
temperature and humidity.
•Methodology/Operating Procedure
Prestart-up Guidelines
• Liquid distributor be correctly mounted noting
  the wheel be rotating freely

• Air
    must be made sure that its not sucked into
 the dryer system due to air leakage

• Initial
       weight of the collection jar be noted and
 fastened securely
•Methodology/Operating Procedure
• Compressed   air 5 – 6 kg /cm2 (70 – 90 lbs/in2)
 supplied

• Air
    hose attached to the stud located at the
 back of the instrument panel

• Oil
    or water separator must be placed I the
 compressed air line
•Methodology/Operating Procedure

• Prepare    slurry containing 30% by mass
 detergent

• Weight of dry solids and weight and slurry
 before drying
•Methodology/Operating Procedure
Startup
• Open the spray dryer unit by turning on the
  power

• Operation   switch from 0 to M to start the fan

• Switch turned to either I, II or III depending on
 inlet air temperature required. Use % timer to
 desired air temperature
•Methodology/Operating Procedure
• With  the heater on and the fan started, the
 atomizer be started by completely opening the
 air valve

• Distilled
          water be passed to the atomizer until
 required outlet air temperature obtained

• Switch
       to feed slurry after obtaining desired
 temperature
•Methodology/Operating Procedure

Main Experiment

• Feed the slurry and air temperature at a
 constant rate together
•Methodology/Operating Procedure
Following Experimental data be gathered
   • Inlet air temperature, Ti

   • Outlet Air Temperature, Tc

   • Operating Pressure of Atomizer

   • Absolute Humidity of air at Ti

   • Absolute humidity of air at To

   • Inlet Temperature of solids, T’

   • Air Velocity

   • Total Run Time
•Methodology/Operating Procedure

• Replacethe Collecting jar after approximately
 ten minutes after the contents runs out

• Repeat the process for another feed rate by
 varying the opening of feed container
•Methodology/Operating Procedure
Shut Down

• Switch
       to distilled water noting and regulating
 the amount of water fed

• Run   the unit for another 5- 10 minutes

• Switch
       off the heater, set the % timer to zero,
 and operation switch at M
•Methodology/Operating Procedure

• Turnoff the water supply and turn off atomizer
 3 minutes later

• Introduce   cold air through the dryer for 5
 minutes

• After
      the retained powder have been swept
 when air temp is 50 C, turn off operation to
 zero
•Preparation of Detergent Slurry


                  x
      30              100
                x 250
THANK YOU!! 

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C1: Calculating Heat Effects and Efficiency of a Spray Dryer

  • 1. Problem C1: Spray Drying Katipunan, Hazel E. Lizardo, Syreanne C. Maniego, Carlo P. Revalo, Orly M. 5ChE-A
  • 2. • Objectives  To calculate the heat effects involved in the operation of a spray dryer  To determine the efficiency of the spray dryer used in terms of percentage recovery of the dried solids.
  • 3. •Equipment / Materials Spray Dryer with Atomizer 220 V Air Compressor Anemometer Cotton Detergent
  • 4. •Equipment / Materials Stirring Rod Collecting Jar 500-mL beaker Distilled Water Timer
  • 6. •Theory Spray Dryer • Liquid feed is pumped into a spray-disk atomizer. • Droplets are formed inside cylindrical drying chamber. • Cooledgas is drawn by an exhaust fan through a horizontal discharge line set in the side of chamber.
  • 7. •Theory Spray Dryer • Exhaust air passes through cyclone separator. • Dry solids settles out of the gas into the bottom of the chamber.
  • 8. •Theory Advantages of Spray Dryer: • Very short drying time • Production of hollow spherical particles • Desired consistency, bulk density, appearance, and flow properties of products may obtained easily compared to other dryers
  • 9. •Theory • Yieldingfrom a slurry, in a single step, dry product is ready for package • May combine the functions of evaporator, classifier, dryer, crystallizer, or size reduction unit.
  • 10. •Theory Disadvantages of Spray Dryer: • It is bulky and large equipment. • It is not always easy to operate. • Bulk density of dry solid is often difficult to kept constant.
  • 11. •Theory Wet Bulb Temperature • Is the steady-state, non- equilibrium temperature reached by a small mass of liquid exposed under adiabatic conditions to a continuous stream of gas
  • 12. •Theory Method of measuring the wet bulb temperature: •A thermometer or other temperature- measuring device is covered by a wet wick, which is saturated with pure liquid and immersed in a stream of gas having definite temperature and humidity.
  • 13. •Methodology/Operating Procedure Prestart-up Guidelines • Liquid distributor be correctly mounted noting the wheel be rotating freely • Air must be made sure that its not sucked into the dryer system due to air leakage • Initial weight of the collection jar be noted and fastened securely
  • 14. •Methodology/Operating Procedure • Compressed air 5 – 6 kg /cm2 (70 – 90 lbs/in2) supplied • Air hose attached to the stud located at the back of the instrument panel • Oil or water separator must be placed I the compressed air line
  • 15. •Methodology/Operating Procedure • Prepare slurry containing 30% by mass detergent • Weight of dry solids and weight and slurry before drying
  • 16. •Methodology/Operating Procedure Startup • Open the spray dryer unit by turning on the power • Operation switch from 0 to M to start the fan • Switch turned to either I, II or III depending on inlet air temperature required. Use % timer to desired air temperature
  • 17. •Methodology/Operating Procedure • With the heater on and the fan started, the atomizer be started by completely opening the air valve • Distilled water be passed to the atomizer until required outlet air temperature obtained • Switch to feed slurry after obtaining desired temperature
  • 18. •Methodology/Operating Procedure Main Experiment • Feed the slurry and air temperature at a constant rate together
  • 19. •Methodology/Operating Procedure Following Experimental data be gathered • Inlet air temperature, Ti • Outlet Air Temperature, Tc • Operating Pressure of Atomizer • Absolute Humidity of air at Ti • Absolute humidity of air at To • Inlet Temperature of solids, T’ • Air Velocity • Total Run Time
  • 20. •Methodology/Operating Procedure • Replacethe Collecting jar after approximately ten minutes after the contents runs out • Repeat the process for another feed rate by varying the opening of feed container
  • 21. •Methodology/Operating Procedure Shut Down • Switch to distilled water noting and regulating the amount of water fed • Run the unit for another 5- 10 minutes • Switch off the heater, set the % timer to zero, and operation switch at M
  • 22. •Methodology/Operating Procedure • Turnoff the water supply and turn off atomizer 3 minutes later • Introduce cold air through the dryer for 5 minutes • After the retained powder have been swept when air temp is 50 C, turn off operation to zero
  • 23. •Preparation of Detergent Slurry x 30 100 x 250

Hinweis der Redaktion

  1. Consists of vertical cylindrical chamber into which the liquid solution is dispersed into a stream of hot gas in the form of fine droplets.Flow of the liquid and gas may be counter current, co-current, or a combination of both