The document provides an overview of dehydration principles and technologies. It discusses: - The history of food dehydration dating back 5000 years and developments through World Wars I and II. - Key concepts in dehydration including moisture transport mechanisms, drying curves, kinetics, equilibrium moisture content, and factors that influence the process. - Common drying technologies classified by operation mode, pressure, heat transfer mode, and product state. Advantages and disadvantages of different methods are described. - Quality aspects of dehydrated foods regarding physical properties, microbiological and chemical changes, and nutritional impacts. Drying methods and pretreatments can influence quality.

1. Chapter 1: General
Concepts in Dehydration

2. Introduction
• Dehydration or Drying is a processing method or
preservation method?
• What the purposes of food dehydration?

3. Introduction
• Persian and Chinese people dried fruits and vegetables in the sun as
long as 5000 years ago.
• The 18th century: used artificial energy with controlled drying
conditions: Vegetables were soaked in hot water and conduction
drying.
• Continuing to develop in World War I and II.
• During World War I and II: continue to develop other drying
methods such as vacuum drying (fish meat), drum drying (butter,
soup, tomato paste), spray drying (milk and eggs).
• 1960s: Development of sublimation drying.

4. Introduction
• Due to high demands of customers (high quality,
low price, etc.), many novel drying technologies
(microwave, ultrasound, heat pump, etc.) have been
researched and developed.

5. Theoretical considerations of air-
water mixtures
• The dehydration process depends on understanding the relationship
between the water contained in a foodstuff and the water present in the
drying medium, which is usually air.
• Ideal gas equations for air and water are as follows:
PV = n RT
P: the partial pressures; n: the number of moles; V: the total volume; R: the gas
constant; T: the absolute temperature.
• If the mixture consists only of air and water, the total pressure (Pt ) is
the sum of the water and air partial pressures (Dalton law):
Pt = Pa + Pw
Pa và Pw: are the partial pressures of air and water in the mixture, respectively

6. Absolute humidity
• The mass ratio of water to dry air is known as the absolute
humidity, which can be defined as the amount of moisture in
the air at any condition (Y ):
Mw và Ma: are the molecular weights of water and air, respectively.
• Dry air (78% nitrogen, 21% oxygen, and 1% other gases) has
an average Ma of 29 Da and water has an Mw of 18 Da.

7. Saturation Absolute Humidity
• The mass ratio of water to air is called the saturation
absolute humidity.
Pw0: is the saturation vapor pressure of water.

8. Relative humidity
• is defined as the ratio of Pw to Pw0 at the same
temperature.
• It is a relative measure of the amount of moisture
that wet air can hold at a given temperature:

11. Psychrometric or humidity chart
• The psychrometric chart is very useful for heat and mass
balance determinations involving air–water mixtures.
• Psychrometric consists of:
o Dry bulk temperature
o Wet bulk temperature or
saturation temperature
o Dew point temperature
o Absolute and relative
humidities
o Enthalpy (total heat)
o Specific volume

12. http://www.sp.uconn.edu/~mdarre/NE-127/NewFiles/psychrometric_inset.html

13. Terms
• Dry bulb temperature: ambient temperature, not affected by
moisture content
• Wet bulb temperature: temperature of adiabatic saturation

14. • Dew point temperature: the temperature at
which water vapor starts to condense out of
the air.
• Relative humidity: measure of the amount of
water air can hold at a certain temperature.
• Humidity ratio of moist air: weight of the
water contained in the air per unit of dry air.
• Enthalpy: heat energy content of moist air.
• Specific volume: the space occupied by air.

15. Drying
• Heated air at 50oC and 10% RH is used to dry rice in
a bin dryer. The air exits the bin under saturation
conditions. Determine the amount of water
removed per kg of dry air.

17. Dry bulb and wet bulb temperature

18. Relative humidity

19. Dew point temperature

20. Enthalpy

21. Specific volume

24. Questions
• Question 1: Given the ambient temperature is 70°F measured by
a dry bulb thermometer and 60°F measured by a wet bulb
thermometer, what is the relative humidity?
• Question 2: An air conditioning system is not working well. The
temperature of the evaporator coil is 53°F. The air in the room is
at 76°F and 40% relative humidity. Will the air conditioner
remove moisture from this air?
• Question 3: A house is 4500 ft2 and has 12 ft ceilings. For
comfort, the home owner specifies 0.3 changes of air per hour.
The outside air temperature is 90°F dry bulb and 73.5° wet bulb.
The air indoors is 75°F dry bulb 50% relative humidity. What is
the amount of cooling required to provide the fresh air?

25. DEHYDRATION PRINCIPLES
• A wet material placed in a medium having lower water
partial pressure (at the same temperature) will dehydrate
until equilibrium is reached.
• The medium is usually air at pressures ranging from a high
vacuum to atmospheric (or higher), although superheated
steam, hot oil, solvents, and solutions may also be used.
• Food dehydration is a complex phenomenon involving
simultaneous mass and energy transport in a hygroscopic
and shrinking system.

26. DEHYDRATION PRINCIPLES
• Heat transfer from the drying medium to the wet solid can be a
result of:
• convection,
• conduction,
• radiation effects,
• a combination of them (in some cases)
• Internal heat transfer is usually very rapid compared to external
transfer;
• Mass transfer depends on either the movement of moisture within
the solid or the movement of water vapor from the solid surface to
the bulk medium.
• Internal mass transfer is generally recognized to be the principal rate-
limiting step during drying.
• The structure of food material being dried plays an important role in
the mechanism of water movement within a product

27. DEHYDRATION PRINCIPLES
• Liquid materials and gels: water transport is by molecular
diffusion from the interior to the surface of the product,
where it is removed by evaporation.
• Capillary-porous materials: the possible physical
mechanisms are numerous and can be classified as
1) liquid movement caused by capillary and gravity forces,
2) liquid diffusion caused by a difference in concentration,
3) surface diffusion,
4) water vapor diffusion caused by partial pressure gradients,
5) water vapor flow under differences in total pressure,
6) flow caused by an evaporation–condensation sequence

29. DEHYDRATION KINETICS
• The drying kinetics of the product are the most important
data required for the design and simulation of dryers.
• Drying kinetics are affected by:
v the external conditions of the medium
v the chemical and physical structure of the food
• In the most general case, drying a food under
constant conditions is considered in order to obtain the
kinetics curve.

30. Drying curves as a function
of drying time:
(a)drying kinetics
(b)(b) drying rate.

31. • Free moisture content, Xf:
Xf = X – Xe
(X: Moisture content in db, Xe: equilibrium moisture content).
• Drying rate, Nw, kg water/m2/h):
ms: the mass of the dry solids
A: the area available for drying.

32. DEHYDRATION KINETICS
• The drying rate depends on
üthe heat and mass transfer coefficients,
üdiffusion coefficients,
üthe nature of the food,
üand the external drying conditions.
• Optimization of any or all of these factors would result in
increased drying rates.

33. DRYING TECHNOLOGIES
• Selection criteria for classification of dryers:
1. Mode of operation (batch or continuous)
2. Operating pressure (vacuum, atmospheric, and high pressure)
3. Mode of heat transfer (conduction, convection, radiation,
dielectric heating, and combination of different modes)
4. State of product being dried (stationary, moving, agitated,
fluidized, and atomized)
5. Residence time (short: below 1 min, medium: 1–60 min, long:
higher than 60 min).
6. Cost
7. Quality of end product
8. Safety
9. Ease of design and operation

34. Classification of dryers according
to heat mode transfer

35. ADVANTAGES AND DISADVANTAGES

36. ADVANTAGES AND DISADVANTAGES

37. Quality aspects of dehydrated foods

41. Water sorption isotherms
Equilibrium
moisture
content,
Xe

42. Water sorption isotherms
• Sigmoidal
• hysteresis

43. Hysteresis
Gas-liquid absorption (a) and liquid-solid adsorption (b) mechanism.
Blue spheres are solute molecules
(a) (b)

44. Hysteresis
• Many theories and hypotheses have been formulated to
explain the phenomenon of hysteresis.
1. the nature of the food,
2. temperature, storage time,
3. adsorption - desorption cycles.

45. Temperature effect on sorption isotherms
• Water activity changes with temperature . Thus, water sorption isotherms must also
exhibit temperature dependence.
• A temperature increase results in a decrease of the amount of water adsorbed.
• The effect of temperature on water sorption isotherms is often represented by the
Clausius–Clapeyron equation:
Qs is the net isosteric heat or heat of sorption, which is defined as the difference
between the total molar enthalpy change and the molar enthalpy of vaporization.
R is the universal gas constant.

46. Effect of temperature on water
sorption isotherm for carrot

47. Relationship between Aw and Moisture content
X: moisture content (% dry basis); Xm: monolayer value (% dry basis); T:
temperature (K); C, K, A, B, K1, K2, n1, n2: constants.

48. Physical Properties
• Physical properties such as color, texture, density, porosity,
rehydration capacity are affected by drying methods.

49. Microbiological and chemical quality

50. Nutritional Quality
• Discussion ???

51. Influence of Drying Methods
and Pretreatments