SLIDE 1 TECHNO-ECONOMIC STUDY OF SIMPLIFIED COOLING TIME ESTIMATION METHODS APPLIED ON TWO-PHASE YOGURT MANUFACTURING TECHNOLOGY
- M. Okulić, M. Ožegović and I. Zlatanović
University of Belgrade – Faculty of Agriculture ICR2015 Yokohama, Japan
IIR Student Competition – International Congress of Refrigeration ICR2015 ICR2015 Yokohama, Japan
SLIDE 2
COOLING TIME ESTIMATION IMPORTANCE ?
More efficient and economical operation of the
cooling system for specific technology requirements;
Smaller capacity of refrigeration systems; Energy savings; Cost-effective production process.
SLIDE 3
IMPORTANT PARAMETERS
Thermo-physical properties of food
(heat conductivity, density and heat capacity)
Packaging material (size and shape)
(plastic cup, carton box, cellophane, ...)
Cooling medium
(water, air,...)
Refrigerant propeties
SLIDE 4
SIMPLIFIED COOLING TIME CALCULATION METHODS
1. Cooling time estimation method based on f and j factors 2. Cooling time estimation method based on „Equivalent Heat Transfer Dimensionality“ (EHTD)
SLIDE 5 Cooling time estimation method based on f and j factors
f and j factors represent the slope and intercept, of the temperature history curve. Factor j is a measure of the lag between the onset of cooling and the exponential decrease in the temperature of the food. Factor f represents the time required to
- btain a 90% reduction in the non-
dimensional temperature difference (Y).
10 20 30 40 50 60 0.1 0.2 0.3 0.4 0.6 0.8 1.0 2.0 f j
a i a
T T Y T T , min. Y
ln 2.303 f Y j
SLIDE 6 Calculation of f and j factors for irregulary shaped products
– shape factor – f factor – j factor
2 2 2 1 4 2
1 1 8 3 25 . A A L G
2 1 2
303 . 2 M L f
2 1
0388 .
892 .
M
e j
H A1 A2 L
SLIDE 7 Cooling time estimation method based on „Equivalent Heat Transfer Dimensionality“ (EHTD)
Cooling time estimation method based on EHTD is based on the comparison of the total heat transfer to the heat transfer through the shortest dimension.
2 2
3 ln c L j E Y
4 3 4 3
1.85 1.85 Bi E Bi E E
SLIDE 8 Typical diary supply chain scheme
Farm Transport Diary
(processing factory)
Transport Distribution depots Transport Consumer Cold chain Retail
SLIDE 9 Two-phase yogurt manufacturing technology
Reception
Filtration Separation Cream Skim milk Standardization
to acheive the desired % of fat content
Pasteurization
30 min at T=85oC 10 min at T=95oC
Homogenization
mixing at 15 Mpa and cooling to T=43oC
Starter culture insertion
at T=43oC
SLIDE 10
Small blast freezers Storage cold room
SLIDE 11
Yogurt palette packaging Small blast freezer interior
SLIDE 12 CALCULATION RESULTS Estimation method based on f and j factors
Input data: Cooling time: 56.58 minutes
- Dimension of yogurt cup (diameter 2∙L and height H)
Ø55 x 63 mm
- Shortest distance between cup center and cup surface
L=0.0275 m
- The minimum cross sectional area containing L
A1=0.02375 m2
- The cross sectional area that is orthogonal to A1
A2=0.003465 m2
Bi=1.368
G=0.801
M1
2=1.48
f=13169
j=0.842
- The fractional unaccomplished temperature difference
Y=0.465
SLIDE 13 CALCULATION RESULTS Estimation method based on EHTD
Input data: Cooling time: 53.11 minutes
L=0.0275 m
Bi=1.368
ω =1.776
E0=2.74
E∞=2.04
- (second shortest dimension of food item)/(shortest
dimension of food item) β1=1.15
- (longest dimension of food item)/(shortest dimension of
food item) β2=1.15
j=0.842
- The fractional unaccomplished temperature difference
Y=0.465
SLIDE 14
The yogurt cup radius variation impact on cooling time
SLIDE 15
CONCLUSION
Simplified cooling time calculation methods represents very usefull and reliable tool for the refrigeration system dimensioning.
Dimension, shape and geometry of cooled product has great influence on cooling process.
The type and form of packaging must be considered during the product design phase, when the application of these methodes can be of importance.
This will bring financial savings in the production process due to the higher energy efficiency of the system.