Thermal treatment for products
Thermal treatment is normally applied to the product to reduce its microbial load and guarantee the required shelf life. Heat acts on the proteic structures inside the microorganism cells and can kill the microorganism or deactivate its reproduction capability. Effectiveness of a heat treatment is normally expressed in pasteurizing unit:

K = constant,
ts = sterilization time in minutes
Ts = sterilization temperature in °C.
Heating and cooling time are not considered in the determination of the heat treatment time, although they contribute to the sterilization performance. Thus, holding time and not heating time is used as a treatment parameter. Temperature is the most effective microorganism killing agent and the most relevant treatment parameter. Its sterilizing effect is growing exponentially when temperature is raised. High efficiency can be reached from 80°C upwards. For example, 100 P.U. can be applied to orange juice by treating it at 130°C for 1 second holding time or by treating it at 90°C for 50 seconds holding time. It is normally necessary to make compromises between treatment parameters and product decay after treatment to determine a treatment that allows the product to reach the required shelf life at the lowest possible decay of organoleptic properties. P.U. are useful to compare different treatment and determine their overall efficiency, but analysis of the actual product according to reference microorganisms is necessary to determine the actual killing action of a given treatment.



Where K is the reaction speed constant, depending from reference microorganism, temperature and environment conditions.
By integrating between t1 = 0 and t2 = t we obtain:


Switching from natural logarithms to base 10 logarithms and highlighting N = N0 / 10 we obtain:

where D (decimal reduction time) represents the timeframe where the number of microorganisms is reduced by a factor of 10.
By substituting the found value we obtain the first Law of Bigelow:

Values for D change according to the different reference microorganism. The higher the value of D, the more resistant is the microorganism.
We can infer from the First Law of Bigelow that a longer time is required if N0 is a big number.
Moreover, it is not possible to completely kill all microorganisms, as this would imply an infinite treatment time. Killing time becomes shorter as the treatment temperature becomes higher (see "Graphic representation of Second Law of Bigelow").
The inclination of TDT is represented as z, equal to the number of degrees needed to reduce D by a factor of 10. The relation between D(t) and z can be expressed as:


This second law enables us to know the value of D at the required temperature if we know D121°C and z.
For example, we know that for Clostridium botulinum z is equal to 10°C and D121°C value is 0.2'; we can then calculate the value for D at the temperature of 100°C:


n is defined as the number of log reductions.
For a temperature of 121°C we obtain

From a technical point of view FTz is the sum of the killing contribution of each temperature for the microorganisms hosted inside the foodstuff; in other words it is the integral of the heat penetration curve.
The killing action is defined as the relationship between F0 and FTz.


Graphic representation of Second Law of Bigelow

Índice
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Introduction
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1.Markets, opportunities, a comparison of the technologies
- 1.1. “High acid” and “Low acid” beverages
- 1.2. Juices and Nectars
- 1.3. Sport Drinks
- 1.4. Tea and infusions
- 1.5. Functional Beverages
- 1.6. Milk-based products
- 1.6.1. UHT Milk
- 1.7. Historical perspective: Evolution of the technology from the Roman era to our day and age
- 1.7.1. "Aseptic" technology in the Roman era
- 1.7.2. The Roman "filling, capping and storage process"
- 1.8. Technologies to meet market demand
- 1.8.1. Use of preservatives
- 1.8.2. Hot fill
- 1.8.3. Ultra-clean filling
- 1.8.4. Aseptic Filling
- 1.8.5. Aseptic Blow Filling
- 1.9. Advantages and disadvantages of containers for beverages
- 1.9.1. Glass
- 1.9.2. Polylaminate carton
- 1.9.3. PET
- 1.9.4. HDPE
- 1.9.5. Cans
- 1.9.6. Pouches
- 1.10. Caps, closures, fitments
- 2.The right direction of sustainability
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3.Thermal treatment for product
- 3.1. Heat Exchangers for Liquid Products
- 3.1.1. Plate Heat Exchanger
- 3.1.2. Single Tube Heat Exchanger
- 3.1.3. Multi Tube Heat Exchanger
- 3.1.4. Triple Tube Heat Exchanger
- 3.1.5. Spiral Tube Heat Exchangers
- 3.1.6. Scraped Surface Heat Exchangers
- 3.2. Indirect and Direct Heating
- 3.3. Direct Heating UHT and ESL Designs
- 3.3.1. Direct Injection
- 3.3.2. Direct infusion
- 3.4. The best heat exchanger for your application
- 3.4.1. Heat Damage to food
- 3.4.2. System Selection Criteria
- 3.5. Conclusions
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4.Understanding aseptic filling technology
- 4.1. Aseptic technology: an integrated system, not a series of connected machines.
- 4.2. Structure of an aseptic filling line
- 4.2.1. Sterilization
- 4.2.2. Container sterilization
- 4.3. Treatment of containers
- 4.3.1. Peroxyacetic Acid (POAA or PAA)
- 4.3.2. H2O2
- 4.4. PAA WET container sterilization
- 4.5. PAA vapour container sterilization
- 4.6. H2O2 CHP container sterilization
- 4.7. H2O2 VHP container sterilization
- 4.8. Preform sterilization technology
- 4.8.1. CHP sterilization
- 4.8.2. VHP sterilization
- 4.9. Cap sterilization technology
- 4.9.1. PAA spray sterilization
- 4.10. PAA immersion sterilization
- 4.10.1. CHP sterilization
- 4.10.2. VHP sterilization
- 4.10.3. Pre-sterilized caps handling
- 4.11. Energy-based sterilization without chemicals
- 4.11.1. UV light sterilization
- 4.11.2. Pulsed light sterilization
- 4.11.3. Ionizing radiation Sterilization
- 4.11.4. Electron beam sterilization
- 4.12. Aseptic Filling
- 4.12.1. Volumetric electronic filling
- 4.12.2. Weight filling
- 4.12.3. Other filling technologies
- 4.13. Capping
- 4.14. Bottle handling
- 4.15. Ancillary process equipment
- 4.15.1. Sterilizing solution production
- 4.16. Sterile water production
- 4.16.1. Utilities and fluids handling
- 4.16.2. CIP, SIP, COP, SOP
- 4.16.3. Integration of ancillary process units
- 4.16.4. Piping
- 4.16.5. Simplification of line handling
- 4.16.6. Radiation-based fluids sterilization
- 4.17. Line automation
- 5.Your new Aseptic Line
- 6.Good maintenance: the best way to preserve the value of the investment
- 7.Improved safety: for the product, for operators and for the environment
- 8.Aseptic filling and FDA
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9.Sell Aseptic to sell "more" and sell "better"
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10.The Future of Aseptic
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Conclusions
- Addendum