04 the multipurpose fruit factory
DESCRIPTION
fruitTRANSCRIPT
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THE MULTIPURPOSE FRUITS FACTORY MODELSpeaker Francesco Caponetti - Corporate Key Account
Mr. Mario Gozzi R&D manager CFT S.p.A.
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The multipurpose fruits factory model.
Energy consumption for a traditional fruit juice line.
Energy savings and flexibility in CFT technologies:
- Extraction: Zenith fruit puree cold extraction technology.
- Evaporation: Apollo falling film and Poseidon TVR evaporators.
- Aseptic filling: Macropak AF/2.
INDEX
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The multipurpose fruits factory model
Freshfruits
Purchaseraw fruits
Logisticinlet
ProcessWashing
andsorting
Extraction Evaporation Asepticconditioning
Logisticoutlet
Storage Selling
Conclusion:Fruit juice lineFruit puree lineFruit preparation line
3 different products 1 similar know-how
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Energy consumption for a 6 t/h fruit juice line
Conveyingfrom storage
Washingand sorting
Millingheating
enzymation
Juiceextraction
Juiceclarification Evaporation Sterilization andaseptic filling
Electric consumption (Kw) Steam consumption (10x Kg/h)
140
120
100
80
60
40
20
0
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Extraction
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Overview of traditional technologies for fruit juices extraction
Hot extraction + decanter.
Mill + belt press.
Mill + hydraulic press.
Destemmer crusher + membrane press (for pomegranates and grapes).
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Extraction: summary of characteristics in traditional technology
Inactivation delay.
Adding of high quantities of ascorbic
acid to preserve color (for cloudy juice).
Single product oriented lines.
Open air environment:
- Possibility of contamination
Necessity for manual CIP.
Batch pressing operations.
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Extraction: target for new technology
Reduce the consumption of ascorbic acid.
Increase product consistency and reduce syneresis.
Preserve color.
Maintain aroma and other organoleptic properties.
Stabilize final product to achieve better shelf-life.
Stabilize semi-finished product to separate in season
from off season activities.
Multipurpose high flexibility lines.
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Extraction: target for new technology, where to act
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Extraction: apple puree ultra fast anaerobic extraction
Partially O2Elimination
Inactivationof Mash
Cold Extraction
Inactivation ofClean Puree
O2Elimination
Cold Extraction
Inactivation ofClean Puree
Hot Extraction (with cooker)
Time (sec.)
Cold Extraction
Zenith: Ultrafast Anaerobic Extraction
0,5 1,0 1,5 600 600,5
Inactivation Delay
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Enzymatic Browning Reactions*
* Source: Processing Fruits Edited by Diane M. Barrett, Laszlo Somogyi, Hosahalli Ramaswamy
Extraction: why anaerobic?
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Extraction: why cold extraction?
Fruit Enzyme On Pulp[U/g]
On Peel[U/g]
Peel/Pulp
Apple Golden Peroxidase 0.0042 0.0309 7.36
Apple Golden Pectinesterase 0.374 0.346 0.93
Pear Conference Peroxidase 0.013 0.062 4.68
Pear Conference Pectinesterase 1.028 3.21 3.12
Pear Williams Peroxidase 0.019 0.048 2.50
Pear Williams Pectinesterase 1.703 3.135 1.84
Normally the enzymes concentration in the peel is higher than in the pulp (expecially for the oxydative enzymes).
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Extraction: why ultrafast?
Minutes
A
b
s
o
r
b
a
n
c
e
(
4
2
0
6
6
0
)
n
m
Natural apple color
Addition of 850 ppm VIT.C
Without VIT. C
* Values referred to Golden Delicious apple
absorbance vs inactivation delay*
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0 ppm 200 ppm 400 ppm 600 ppm 800 ppm
Hot
Cold
New
* Values referred to apple puree Golden delicious
Determination of ascorbic acid for color stabilization*
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PATENT PENDING
Zenith technology (embodyment for ultra fast and cold extraction principles)Cross-sectional view
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Zenith embodyment : qualitative comparison between traditional extractions and Zenith technology
Hot Extraction Cold Extraction Zenith
Viscosity
Colour
Molds
Pesticides
Black/Brown specks
Taste
Ascorbic acid free
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Industrial results from a CFT customer in South America
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Product: Williams Pear aseptic pureeBrix: 30/32 Ascorbic Acid: 150 ppm
Color hunter: L (benchmark value 50)
Hunter L,a,b color scale Color hunter: b (benchmark value 10)
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Product: Peach aseptic pulpBrix: 30/32 Ascorbic Acid: 150 ppm
Color hunter: L (benchmark value 47)
Color hunter: a (benchmark value 5) Color hunter: b (benchmark value 28)
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Extraction: industrial results, working cost savings
Ascorbic acid cost savings in Zenith compared to traditional extraction technologies.
Hypothesis:- 40 t/h production. - 24 h/day. - 180 days/season. - 10 Euro/kg ascorbic acid price*.
40*103*24*180*10*(800-150)/106 = 1.123.200 Euro/year
* Buying price in February 2010 for an important european fruit processor
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Specific application of Zenith on juices: New technology scheme
Decanter(First juice
extraction stage)
JUICEOUT
WasteOut
Collection Tank
FRUIT IN
Extractor
Lobe pump
SteamIN
CondensateWater
Concentric tubes heater
Star valve
Star valve
Inert gasinlet
CAKE TOSECOND EXTRACTION
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References: 8 Zenith lines sold from January 2008
Country Application Working capacity
Italy Mediterranean fruits up to 20 t/h
Italy Mediterranean fruits up to 20 t/h
Italy Mediterranean fruits up to 20 t/h
Chile Apple, Pear, Peach, Apricot up to 25 t/h
Belgium Apple, Pear up to 5 t/h
Turkey Apple, Pear, Peach, Apricot up to 20 t/h
Argentina Apple, Pear, Peach, Apricot up to 20 t/h
Russia Apple, Pear up to 15 t/h
France Apple, Pear up to 15 t/h
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Evaporation
Apollo falling film and Poseidon TVR evaporators
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Evaporation: Apollo falling film for clear juice production
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Vapor compressor
APOLLOTECHNOLOGICAL SCHEME
Product heating pipes
Product steams insideseparation chamber
Product recovery tankSeparation chamber
Vapor suction duct
Vapor outlet
Tube bundle heat exchanger
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Apollo: technological highlights
GENTLE TREATMENT Temperature difference between steam and
product lower than 6C. Evaporation temperatures lower than 77C. Overall residence time shorter than 300
seconds. Steam economy 1:16 (value referred to
apple)OPERATIONAL FREXIBILITY Short, fully automated cleaning time (3
hours). Quick product change over cloudy/clear no
fiber contamination from cloudy to clear Simple and quick adjustment of evaporation
capacity by setting compressors rpm. Water removal capacity from 10 t/h to 60 t/h
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Hypothesis:- 24 h/day. - 180 days/season. - 40 t/h water removal.- 0,09* Euro/kWh electricity cost.- 25* Euro/t steam cost.
Traditional 5 effects falling film evaporator:- Steam working cost 1.053.659 Euro- Electricity working cost 75.816 Euro
Total 1.129.475 Euro
Apollo falling film evaporator:- Steam working cost 270.000 Euro- Electricity working cost 231.974 Euro
Total 501.974 Euro Saving: 627.501 Euro* Buying price in April 2010 for an important turkey fruit processor
Apollo: saving compared to traditional falling film technologies
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Poseidon T300 TE TVR
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Juice process flowchart
Puree process flowchart
AlexandraHighlight
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Evaporator for the concentration of both purees and juices. Triple effect falling film juice concentration. Double effect puree concentration. No fiber contamination. High flexibility. No quality compromises: full forced circulation in purees / full falling film in juices.
Poseidon T300 TE TVR
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Aseptic filling - Macropak AF/2
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Macropak AF/2: advantages
Multipurpose format:
- 10 / 20 kg bags
- 220 kg drums
- 1000 / 1500 kg bins
Multipurpose spout: 1 or 2 easily changeable kit.
Multipurpose products: high acid & low acid (with no use
of chemicals agents during aseptic filling).
1 day assembly time.
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Macropak AF/2: 3D head details
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Macropak AF/2: working capacity
High Acid product (bags/h) 100 64 21
Low Acid product (bags/h) 75 50 20
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THANKS FOR YOUR ATTENTION !
The multipurpose fruits factory model
Foliennummer 1Foliennummer 2Foliennummer 3Foliennummer 4Foliennummer 5Foliennummer 6Foliennummer 7Foliennummer 8Foliennummer 9Foliennummer 10Enzymatic Browning Reactions*Extraction: why cold extraction? Foliennummer 13Foliennummer 14Foliennummer 15Foliennummer 16Foliennummer 17Foliennummer 18Foliennummer 19Foliennummer 20Foliennummer 21Foliennummer 22Foliennummer 23Foliennummer 24Foliennummer 25Foliennummer 26Foliennummer 27Foliennummer 28Foliennummer 29Foliennummer 30Foliennummer 31Foliennummer 32Foliennummer 33Foliennummer 34Foliennummer 35