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Unit operations
Raw material selection
Storage of raw material
Cleaning
Sorting
Grading
Peeling
Processors define their requirements in terms of raw material specifications
size
unit per kg
level of maturity
sugar content
Raw material selections
Storage of raw materials governed by
Temperature
Moisture/humidity
Atmospheric composition
Spoilage mechanisms (3)
Living organisms
Biochemical activity
Physical processes including damage
removal of contaminants essential for protection of process equipment and final consumer
Wet procedures - liquid solvents (water and detergents)
dry procedures - lower moisture content
can use water for fruit and veg
should take place at earliest opportunity possible
Examples…
Cleaning
wet - spray washers, brush washers, drum, rod washers
Dry - air classifiers, magnetic separators
Separation of foods into categories based on measurable physical properties
Sorting
size
colour
dimension
Shape and size sorting done by two methods
Flatbed screen
Drum screen
Assessment of overall quality of food using several attributes
Grading
Peeling is used to
remove unwanted or inedible material and improve appearance of final product
flash steam
Knife peeling
Abrasion peeling
Caustic peeling
Flame peeling
Blanching is a .. heat treatment
mild
Blanching process involves
heating food rapidly to a predetermined temp, holding at temp for a specified time then cooling rapidly
Purpose of blanching is to
Inactivate enzymes
remove gas from plant tissues
oxygen for oxidation
helps achieve vacuum in canning
Shrinking and softening of tissue
Final cleaning and decontamination process
Significant reduction in microorganism content
Consequences of blanching
Overprocessing leads to excessive loss of texture
Weight loss from the tissue
Operation in which average size of food is reduced by grinding, compression, impact forces (shearing, tension, compression)
Size reduction
When size reduction applied to liquids it is called
Homogenisation or emulsification
benefits of size reduction to food processing
Surface area to volume ration increased - increases rate of drying, heating, cooling
Allows more complete mixing of ingredients
Control textural particle size
Control rheological properties of food (how materials deform under applied forces)
Negative impacts of size reduction on food quality
Increase in surface area to volume ratio of food means higher contact with oxygen so increased oxidation
3 types of forces used for size reduction of solids
Compression
Impact
Shearing
in most equipments all three are used together
Stress strain diagram for foods
Internal strains are first absorbed up to elastci stress limit E
After E food permanently deformed
B is the breaking point
Size reduction of solids - amount of energy needed to fracture food depends on
Hardness of food
Moisture content
Heat sensitivity
Selection of equipment for size reduction depends on whether a food is
fibrous
smaller pieces or pulps
Dry paticulates or powders
Size reduction of fibrous foods (4)
Slicing - rotating blades
Dicing equipment - two sets of rotating knives
Shredding equipment - hammer mill with knives
Pulping equipment - compression and shearing forces for juice extraction
Size reduction of dry foods (4)
Ball mills - steel balls used to produce fine powder
Disc mills - single or double grooved disc rotating
Hammer mills - swinging hammer inside chamber
Roller mills - two or more rollers in different direction and speed
Effect of size reduction on solid foods
control textural and rheological properties of foods
Improves efficiency of mixing and heat transfer
Effect of size reduction on sensory characteristics of solid foods
Higher oxidation
colour chnages
off flavours
textural changes
Effect of size reduction on nutritional characteristics of solid foods
loss of nutritional value due to oxidation of fatty acids and carotenes
Loss of vit C in chopped and sliced fruits and veg
Size reduction in liquid foods (2 types)
Emulsification
Homogenisation
Emulsification is the formation of
a stable emulsion by intimate mixing of two or more immiscible liquids so that one (dispersed phase) is formed into very small droplets within the second (continuous phase)
Homogenisation is the
reduction in size and hence increase in number of solid or liquid particles in the dispersed phase by application of intense shearing forces
Stability of an emulsion is dependent on
type and quantity of emulsifying agent
Size of the globules in the dispersed phase
interfacial forces acting on surface of globules
viscosity of continuous phase
difference in density of dispersed and continuous phase
4 equipments for homgenising
High speed mixers
Pressure homogenisers
Colloid mills
Ultrasonic homogenisers
equipment to premix emulsions of low viscosity liquids by a shearing action
high speed mixers
Equipment to make droplets even smaller
pressure homogenisers
Equipment used for high viscosity fluids
Colloid mills
Equipment that causes alternate cycles of compression and tension in low viscosity liquids and cavitation of air bubbles to form emulsions with droplet sizes
Ultrasonic homogenisers
What effects viscosity or temperature of liquid foods
type of emulsifying agent
Stabiliser
homgenisations conditions
in milk fat globule size effects cremier texture
Size reduction foods effects
Colour - milk more fat globules = greater light reflectance
aroma
nutritional value
shelf life
Dehydration/drying is the
application of heat under controlled conditions to remove majority of water normally present in a food by evaporation
main purpose of drying
Extend shelf life by reduction in water activity
inhibits microbial growth and enzyme activity
Reduction in weight and bulk of food reduces
transport, storage and packaging costs
Negatives of drying
Highly energy intensive
Causes deterioration of eating quality and nutritional value
Examples of dried foods
Coffee, milk, raisins, pasta, flours, breakfast cereals
Examples of dried ingredients
egg powder, protein powder, flavourings, colourings, yeasts, lactose
Mechanism of drying
hot air blown over wet food, water vapour diffuses through boundary film of air surrounding the food and carried away by moving air
Vapour pressure gradient created as lower water vapour pressure on surface of the food due to hot air
Gradient provides driving force for water removal from the food
3 stages of drying
Settling down period
when drying first starts and surface is heating up
Constant rate period
drying starts
water moves from interior to surface at same rate as evaporation
until critical moisture content reached
rate of drying declines gradually
Falling rate period
movement of water from interior to surface falls below evaporation rate
longest part of drying
most bound moisture removed
3 characteristics of air necessary for successful drying
moderately high dry bulb temp
low RH
high air velocity
2 equipments for drying
Hot-air driers
heated surface/contact driers
Spray driers
A fine dispersion of preconcentrated food is first atomised to form smaller droplets and then sprayed into a co or counter current flow of heated air
Effects of conventional drying on foods
Shrinkage, puffing, crystallisation
loss of fat soluble vitamins
reduction of ascorbic acid and carotenes from heat
decrease in volatile and phenolic compounds
Denaturation of proteins
production of chemical contaminants
Method used to dehydrate heat sensitive foods, process of which is based on sublimation (ice to vapour)
freeze drying
What method of drying produces the highest quality product obtainable?
Freeze drying
4 components of a freeze dryer
drying chamber
vacuum pump
heat source
a condenser
3 stages of freeze drying
initial freezing - crucial for size shape and distribution of ice crystals and hence the final structure of freeze dried foods
primary drying
secondary drying
Advantages of freeze drying
porous non- shrunken structure that can be rehydrated
Preserves sensory and some structural characteristics
Disadvantages of freeze drying
expensive
High energy consumption
Transformation of feed from a fluid state to a dried form by spraying feed into a hot drying medium
Spray drying
Spray drying parts and process
Feed is pumped to atomizing device (surface area increased)
Drying air drawn from atmosphere and filtered and heated - injected from top or bottom of sprayer
Droplets meet hot air and evaporation takes place
dried product falls to bottom of chamber
Air is passed through cyclones to remove fines (small particles)
Advantages of spray drying
Broad application and capacity
powder quality remains constant
Operation is continuous (can be done for days without stopping)
Variety of spray dryer designs
Basic summary of spray drying
Concentration
Atomization
Droplet-air contact
Droplet drying
Separation
Concentration stage of spray drying
increases the solid content and reduces amount of liquid needing to be evaporated
Atomization stage of spray drying
creates optimum conditions for spray drying to occur (increases surface area to volume ratio) - leads to a product having desired characteristics
Different nozzles
Pressure nozzle
Rotary nozzle (spraying and rotating)
Droplet-air contact stage of spray drying
atomized liquid brought into contact with hot air
evaporation of 95% of liquid occurs in a few seconds
way spray contacts air will influence behavior of droplets and dried product - position of hot air inlet
Droplet drying stage of spray drying (2 stages)
Stage 1: sufficient moisture in drop to replace liquid evaporated at surface - constant rate
Stage 2: no longer enough moisture to maintain saturated conditions - dried shell forms on surface - rate falls rapidly
Separation stage of spray drying
Particles fall to bottom of chamber
Some particles remain in air and are removed using cyclones and other separation equipment
Co-current flow spray dryer
Used for??
Product and drying air introduced in the chamber in same place
for heat sensitive products because hottest air contacts droplets at highest moisture content
Counter current flow air dryer
Material and the air are injected at opposite locations of the drying chamber
not suitable for heat sensitive products
Mixed flow spray dryers
combo of co current and counter current spray drying
hot air introduced at top and material from the bottom
lower drying rate and denser product
Spray dryers can be…and… cycle layout
open
air put into environment after use
closed
filters applied after feed is dried and extracted
air put back into system
Low temperature does not destroy microorganisms or enzymes but
depresses their activity
Low temp is not a method of
permanent preservation
It cannot improve the initial quality of a product
2 low temp processes are
chilling and freezing
Freezing means a lower temp but also
depression of water activity due to water being in solid state
Arrhenius equation
describes relationship between temperature and rate of chemical reactions (higher temp = faster rate of reaction)
Low temp and enzyme activity
enzyme activity slowed but not eliminated by refrigeration
Low temp and microorganisms
psychrophiles are of biggest concern as better growth between -10-15 degrees
At low temp lag phase is longer and logarithmic phase is longer (growth is slower)
Low temp and biological activity (respiration)
control the rate of respiration
Greater preservation effects when chilling used in conjunction with
other unit operations (control of gas composition)
reduce O2 when chilling fruit to reduce respiration
Controlled atmosphere conditions
modification of normal gas composition to control respiration rate
CAS - controlled atmosphere storage
MAS - modified atmosphere storage
MAP - modified atmosphere packaging
CAS monitors and regulates
O2, CO2 and ethylene
MAS - gas composition is
allowed to change by normal respiratory activity of the food
MAP - gas composition of packaging is
altered after food put in and before packaging sealed
Two methods of chilling (equipment)
Mechanical refrigerators
compressor sucks gas, compresses then converts to high temp liquid which is cooled by condenser which then passed back to the refrigerator
Cryogenic systems
cyrogen changes phase by absorbing latent heat to cool food
solid or liquid CO2 and liquid nitrogen
Chilling causes ….in nutritional properties of food
little or no reduction
Freezing is
one of the most beneficial preservation methods
lowers aw
Freezing curve A-B
Food cooled below freezing point - supercooling
Freezing curve B
nucleation or ice crystal formation
Freezing curve B-C
Temperature rises as ice crystals being to form and latent heat of crystallisation released
Freezing curve C-D
Ice crystallisation
solutes become concentrated so temp must decrease
Freezing curve D-E-F
crystallisation of water and solute continues
all water that is bound becomes ice
Freezing equipments methods
mechanical refrigerators
cryogenic systems
Two types of freezing (rates)
Slow freezing
ice crystals grow in intercellular space and deform/rupture cell walls
Ice crystals have lower water vapour pressure so gradient created and water moves from cells and cells become dehydrated
Fast freezing
smallers crystals both within cells and in intercellular space
little physical damage to cells as no water vapour gradient created
Biochemical changes in food from freezing
Degradation of pigments
loss of vitamins
residual enzyme activity
oxidation of lipids