thin film evaporation and drying
TRANSCRIPT
Thermal Separation Technology VM/MKA / 13.5.20141
OFITechnical / Scientific
Conference
ISTANBUL
Tuesday May 13, 2014
Thermal Separation Technology VM/MKA / 13.5.2014
Thin Film Evaporation and DryingThin Film Evaporation and Drying
An advanced technology for treatmentof
edible oils, fats
and related products
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Evaporation and Drying Technology
General Definition:
Transition from liquid to vapor phase
Related to our applications:
Separation of volatiles frommixtures or relative thin slurriesby evaporation of this fraction.
The remaining product will bea liquid or a dry product.
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Properties of sensitive products:
• Heat sensitivity
• Viscosity
• Foaming
• Fouling
• Solids in product
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Requirements for gentle separation process bythermal evaporation:
• Short residence time
• Low temperatures
• High heat flux
• High evaporation rates
• Continuous agitation of the film forcleaning and heat transfer purpose
This leads to Thin Film Evaporation and Drying technology.
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SMS thin-film evaporation technologyquickly
separates volatiles from less volatile components
using indirect heat transfer and
mechanical agitation of a flowing product film
within a short treatment time
under controlled conditions.
What is Thin-Film Evaporation ?
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Thin Film Evaporator
Feed inlet
Concentrate
Vapour / Distillate
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Thin Film Mechanism
• High film turbulence
• Rapid film renewal
• Increased heat & mass transfer
• Controlled residence time
• High squeezing factor
• Viscosity up to 20 kPa*s
Thin Film Evaporator - Principle
heated wall
thin liquid film
rotor blades
bow wave
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Solution for temperature sensitive products
Special requirements of the product mixture:
• Very high boiling temperature of volatiles• Temperature sensitive components
Very low vacuum has to be applied:
≥ 0,001 mbar (abs)
This pressure range cannot be handled by
Thin Film Evaporators with external condensers!
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Solution: Short-Path Evaporator
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Examples of typical applications in theoleo-chemical industry
LecithinDistilled MonoglycerideGlycerine• Methyl Ester• Fatty Acid• Carotene• Vitamin E• Omega 3 Fatty Acids• Biodiesel drying and distillation• Many others
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Application 1: Lecithin Drying
SOYBEAN OIL
2- 3 % LECITHIN
DEGUMMING
STAGE1 - 4 % WATER
SEPARATOR
STAGE
Degummed
Soybean Oil
DRYING STAGE
BUSS-SMS
THIN FILM DRYERS
Type KH
WATER
TO STORAGE
WET GUMS
WATER : 40 - 60 %
OIL : 15 - 20 %
LECITHIN : 35 - 40 %
Dryed LECITHIN
WATER : 0,3 - 1 %
OIL : 30 - 35 %
LECITHIN : 65 - 70 %
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Lecithin: : Typical Process Flow Diagram
PFAD
Y:\BUECHELH\VERTRIEB\POWER-POINT PRÄSENTATIONEN\PRINCIPAL-LECITHIN-DRYING-PLANT.VSD
Wet
Lecithin
Vacuum
System
MP Steam
Destillate
Dried
Lecithin
Waste
Water
LP Steam
M Lecithin Dryer
LP Cond.
Condenser
Vent
CW Out
CW In
CW In
CW Out
Cooler
H1
H2
H3
P1
P2
P3
V2
V1
VS1
VM-VD/HGB/10-Jul-2006
CW In
CW Out
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Application 2: Distilled Monoglyceride
Monoglyceride is the most frequently applied emulsifier in foods,such as
Mono-Glycerides are also used in composing pharmaceuticalproducts and cosmetics plus a variety of technical applications.
• Bakery products • Ice-cream• Cooking ingredient • Chocolate• Sweets • Packing material for food (cheese)
• Chewing Gum • Pasta etc.• Margarine
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Process Block Diagram Manufacturing of DMG
Glycerine
Fat
Pre-Heating
MonoglyceridePowderSpray Cooling
DistillationSeparation ofGlycerine and
Catalyst
Inter-Esterification Cooling
FluidMonoglyceride
Catalyst
Glycerine
Glycerine
Di-/Triglyceride
DMG > 95%
DMG < 95%
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Distillation Process for DMG
Step 1 Step 3Step 2
Feed Residue
Di- andTriglyceride
Glycerin GlycerinFatty acids
Monoglyceride
Distillate
Pressure 2,5 mbar abs. 0,2 mbar abs. 0,005 mbar abs.
Boiling point ~ 136 °C ~ 130-140 °C ~ 150-160 °C
Heating temperature ~ 180°C ~ 160 °C ~ 185 °C
Solidification point ~ 25-30 °C ~ 68 °C
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Application 3: Glycerine Distillation
Purpose:Producing Glycerine of pharmaceutical grade by Thin FilmEvaporation and Distillation.
Process Steps: Elimination of excessive water to < 1 % Distillation of Glycerine in a special developed distillation
column Squeezing of the column bottom by means of our Vertical
Thin Film Evaporator for the highest Glycerine yield Deodorising of Glycerine Bleaching for pharmaceutical grade
Thermal Separation Technology VM/MKA / 13.5.2014
Block Diagram Glycerine DistillationG
lyc
eri
ne
Pre
-Co
nc
.
Vent
Thin Film
Evap. Typ
CP-Dryer
Purified
Glycerine
De-
Watering
Deo-
Column
Condes.
M.S. Steam
Jets
Column
Reboiler
Salt, Mong,
Glycerine
Waste
waterGlycerine
Distillation
Column
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Pilot test runs
Process design
Basic and detailed engineering
Key equipment manufacture
Quality Control
Assembly supervision -
commissioning
Start-up
After sales services
Buss-SMS-Canzler: Scope of Services
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Thank for yourkind attention!
Visit us at booth D 2