ULTRASOUND PROCESSING IN FOOD
SANTHOSH. R
M. Tech (FPE)
Introduction
• Ultrasound is defined as sonic waves with frequencies more than 20kHz.
• Ultrasound is developed to minimize processing, maximize quality and
ensuring the safety of the food.
• Power ultrasound has been reported to be sufficient to meet the FDA’s
mandatory 5 log reduction of food born pathogens in fruit juices.(Baumann
et al, 2005)
Types
• High frequency low intensity ultrasound
- low energy [less than 1 W/cm²], high frequency [1-10MHz]
- non destructive imaging, diagnostic purposes
• Low frequency high intensity ultrasound
- high energy [more than 10 W/cm²], low frequency [20-100kHz]
- generates strong shear and mechanical forces
- destructing microbes, protein denaturation, stimulating seed
germination, enhancing crystallization
Principle - Cavitation
• When a sonic wave propagates in a liquid media as a longitudinal wave, it
creates alternating compression and expansion cycles.
• When negative pressure in the liquid, created by expansion cycles, is low
enough to overcome intermolecular forces, small bubbles are formed.
• During subsequent expansion/compression cycles, bubbles expand and
contract.
Cavitation
Stable cavitation
• Cavitation that originates from low power ultrasound in small bubbles, the
sizes of which oscillate slightly during thousands of cycles.
• Ultrasound makes bubble vibrate, causing microstreaming that act as
shock waves.
Transient cavitation
• When high power ultrasound hits liquid media, the size of the bubble
oscillates strongly.
• The surface area of the bubble increased during expansion, which also
increases gas diffusion.
• These bubbles, distributed throughout the liquid, grow over a period of few
cycles to a critical size until they become unstable and violently collapse.
• The phenomenon of growth and collapse of microbubbles under ultrasonic
field is known as ‘Acoustic cavitation’
During cavitation
• When cavitation bubbles oscillate and collapse, several physical effects are
generated, namely, shock waves, microjets, turbulence, shear forces, etc.
• The collapse of the acoustic cavitation bubbles is also near adiabatic and
generates temperatures (5500°C) and pressure peaks (10⁵ kPa) within the
bubbles for a short period of time. Under this extreme temperature conditions,
highly reactive radicals are generated.
• These radicals have been used to achieve chemical reactions that include the
synthesis of nanomaterials, polymers, degradation of organic pollutants, etc.
Equipment
• Consists of
Electrical power generator
Transducer
Emitter
• Others systems include liquid whistle [without electrical generator] and
airborne systems [which do not require an emitter].
• Generator provides the required electrical energy to transducer.
• Transducer as a central element, that converts electrical energy into
sound energy by vibrating mechanically at ultrasonic frequencies. Three
types – liquid driven, magnetostrictive and Piezoelectric transducer. Later
is the most common and effective type. Ex - pzt [lead zirconate titanate]
• Emitter/reactor/ultrasonic cell radiates ultrasonic wave from transducer to
medium.
• Two main form of emitters are bath and horns [i.e. probes]
Probe type
• The probe-type sonoreactors feature a high sound intensity (W/cm²) at the
probe surface and a high acoustic power density (APD) (W/cm³) in the
reactor.
• The probe is often in direct contact with the food. Processes that require a
high energy input, such as cell rupturing, extraction, enzyme inactivation,
etc., are often performed with a probe or a radial horn.
• Titanium and silica are used, due of their mechanical strength.
Bath/tank type
• Tank-type ultrasound treatment devices have a lower sound intensity and
APD, due to the larger volume of the liquid in the chamber, as well as the
large surface area that emits the ultrasound.
• Here, Power is often low in order to avoid the cavitation damage to the
tank walls.
• Ultrasonic baths often find application in surface cleaning,
sonocrystallization, freezing and other applications that need a relatively
low APD.
Calorimetry method
• The ultrasound power level or energy that is delivered to food is expressed
as ultrasound power(W), ultrasound intensity(W/𝑐𝑚2
), acoustic energy
density(W/𝑐𝑚3 or W/mL).
𝑃 = 𝑚𝑐 𝑝
𝑑𝑇
𝑑𝑡
𝑈𝐼 =
4𝑃
𝜋𝐷2, D – diameter of probe(cm)
𝑨𝑬𝑫 =
𝑷
𝒗
, v – volume of medium(𝑐𝑚3)
Product variables
• Volume
• Temperature
• Viscosity
• pH
• Soluble solids
• Gas concentration
Process variables – frequency, amplitude cycle, exposure time & Acoustic
energy density.
Effect on microorganisms
• Appropriate ultrasound can promote the growth of microbial cells.
• Low intensity ultrasound provides steady cavitation and causes repairable
damages. It changes the living state of microbial cells leading to accelerate of
their proliferation and more products of metabolism.
• High intensity ultrasound can not provide accelerating proliferation effect due to
its unrepairable damages.
• Resistance to ultrasound in the order of Gram negative bacteria<Gram positive
bacteria<Yeast<spores , depend upon their complex structures.
Inactivation mechanisms
• Bacteria cell wall damage, due to mechanical effects induced by pressure
gradients generated during the collapse of cavitation bubbles within or
near the bacteria.
• Shear forces induced by micro-streaming which occurs in the bacterial cell
itself.
• Chemical attack due to formation of free radicals during cavitation which
attack the cell wall structure leading to disintegration. In addition there will
be the formation of a small amount of hydrogen peroxide via sonication,
which itself is a bactericide.
• Sonication has been less effective to gram positive bacteria such as
Staphylococci aureus and Enterococci due to their tough cell wall
structure.
• Ultrasound is relatively less effective against spores due to their resistance
to damage.
• Yeast cells may be resistant to physical effects of ultrasound because they
are relatively rigid structure and they are not disrupted by microstreaming.
Effect on enzymes
• Acoustic cavitation induced by ultrasound waves, both physically and
chemically affect enzymes.
• Denaturation of protein is highly responsible for enzyme inactivation either
by free radicals in sonolysis of water molecules or shear forces resulting
from the formation or collapse of cavitation bubbles.
• Enzymes such as catalase, yeast invertase & pepsin are resistant to
ultrasound.
• Enzyme inactivation mechanism is complex and depends upon several
factors such as fruit juice composition, pH, enzyme type and processing
parameters.
• Enzyme inactivation increases with increase in solid content and
decreases with increase in enzyme concentration.
• Decrease in inactivation is observed at high fat food molecules.
• Generally, higher enzyme inactivation is reported for probe type systems
than ultrasound baths.
Fruit juice enzymes
• Pectinmethylesterase (PME) – hydrolyses pectin results in reduced
viscosity. (D-value reduced from 45 min to 0.85 min in tomato juice. Lopez,
1998)
• Polyphenoloxidase (PPO) – copper containing enzyme causes enzymatic
browning.
• Peroxidases (POD) – heme containing enzyme causing off-flavors and
browning pigments. Thermally stable.
• Lipoxygenase (LOX) – related to oxidation of fatty acids and pigments.
Dairy enzymes
• Sonication of milk results in a diversity of physicochemical changes in
macromolecules including enzyme inactivation, homogenization, reduction
in fermentation time during yoghurt preparation and improvement of
yoghurt rheological properties.
• Heat resistant lipase and protease were destructed (can withstand UHT).
• Differences observed in the inactivation of the native milk enzymes such
as alkaline phosphatase, γ-glutamyltranspeptidase, lactoperoxidase, whey
proteins (α -lactalbumin and β-lactoglobulin) in whole and skim milk due to
its composition.
• Very less effect of sonication on milk enzymes without high temperature.
Critical Factors
Governing microorganism and/or enzyme inactivation are,
• Nature of ultrasonic waves or amplitude
• Exposure time
• Microorganism or enzyme type
• Volume of food to be processed
• Composition of food
• Temperature
Application
• Application of ultrasound to food processing divided into two categories.
- To replace traditional processing techniques.
- Ex : food cutting, emulsification/homogenization,
pasteurization/sterilization, meat tenderization and degassing, etc.
- To assist the traditional techniques.
- Ex : extraction, freezing, thawing, oxidation, brining, filtration and drying,
etc.
In diary (PU)
-Due to shear forces – viscosity decreases.
-In encaps. Solution containing polymer
(protein) is denatured and absorbed on surface
Of liq. Droplets & radicals cross links proteins
Others
Disadvantages
• The lack of standardization in ultrasound operating frequencies and power
levels makes comparison between different effects were difficult.
• Direct contact between probe and food medium.
• Effect on color & antioxidants has been reported in some sonicated
samples due to degradation of pigments (anthocyanin, ascorbic acid,
lycopene & carotenoid) at high energy levels.
• However, during emulsification and processing of vegetable oils, a metallic
and rancid odor has been detected only for insonated oil and foods.
Thank you

Ultrasound in Food

  • 1.
    ULTRASOUND PROCESSING INFOOD SANTHOSH. R M. Tech (FPE)
  • 2.
    Introduction • Ultrasound isdefined as sonic waves with frequencies more than 20kHz. • Ultrasound is developed to minimize processing, maximize quality and ensuring the safety of the food. • Power ultrasound has been reported to be sufficient to meet the FDA’s mandatory 5 log reduction of food born pathogens in fruit juices.(Baumann et al, 2005)
  • 3.
    Types • High frequencylow intensity ultrasound - low energy [less than 1 W/cm²], high frequency [1-10MHz] - non destructive imaging, diagnostic purposes • Low frequency high intensity ultrasound - high energy [more than 10 W/cm²], low frequency [20-100kHz] - generates strong shear and mechanical forces - destructing microbes, protein denaturation, stimulating seed germination, enhancing crystallization
  • 4.
    Principle - Cavitation •When a sonic wave propagates in a liquid media as a longitudinal wave, it creates alternating compression and expansion cycles. • When negative pressure in the liquid, created by expansion cycles, is low enough to overcome intermolecular forces, small bubbles are formed. • During subsequent expansion/compression cycles, bubbles expand and contract.
  • 5.
  • 6.
    Stable cavitation • Cavitationthat originates from low power ultrasound in small bubbles, the sizes of which oscillate slightly during thousands of cycles. • Ultrasound makes bubble vibrate, causing microstreaming that act as shock waves.
  • 7.
    Transient cavitation • Whenhigh power ultrasound hits liquid media, the size of the bubble oscillates strongly. • The surface area of the bubble increased during expansion, which also increases gas diffusion. • These bubbles, distributed throughout the liquid, grow over a period of few cycles to a critical size until they become unstable and violently collapse. • The phenomenon of growth and collapse of microbubbles under ultrasonic field is known as ‘Acoustic cavitation’
  • 8.
    During cavitation • Whencavitation bubbles oscillate and collapse, several physical effects are generated, namely, shock waves, microjets, turbulence, shear forces, etc. • The collapse of the acoustic cavitation bubbles is also near adiabatic and generates temperatures (5500°C) and pressure peaks (10⁵ kPa) within the bubbles for a short period of time. Under this extreme temperature conditions, highly reactive radicals are generated. • These radicals have been used to achieve chemical reactions that include the synthesis of nanomaterials, polymers, degradation of organic pollutants, etc.
  • 10.
    Equipment • Consists of Electricalpower generator Transducer Emitter • Others systems include liquid whistle [without electrical generator] and airborne systems [which do not require an emitter].
  • 11.
    • Generator providesthe required electrical energy to transducer. • Transducer as a central element, that converts electrical energy into sound energy by vibrating mechanically at ultrasonic frequencies. Three types – liquid driven, magnetostrictive and Piezoelectric transducer. Later is the most common and effective type. Ex - pzt [lead zirconate titanate] • Emitter/reactor/ultrasonic cell radiates ultrasonic wave from transducer to medium. • Two main form of emitters are bath and horns [i.e. probes]
  • 13.
    Probe type • Theprobe-type sonoreactors feature a high sound intensity (W/cm²) at the probe surface and a high acoustic power density (APD) (W/cm³) in the reactor. • The probe is often in direct contact with the food. Processes that require a high energy input, such as cell rupturing, extraction, enzyme inactivation, etc., are often performed with a probe or a radial horn. • Titanium and silica are used, due of their mechanical strength.
  • 14.
    Bath/tank type • Tank-typeultrasound treatment devices have a lower sound intensity and APD, due to the larger volume of the liquid in the chamber, as well as the large surface area that emits the ultrasound. • Here, Power is often low in order to avoid the cavitation damage to the tank walls. • Ultrasonic baths often find application in surface cleaning, sonocrystallization, freezing and other applications that need a relatively low APD.
  • 15.
    Calorimetry method • Theultrasound power level or energy that is delivered to food is expressed as ultrasound power(W), ultrasound intensity(W/𝑐𝑚2 ), acoustic energy density(W/𝑐𝑚3 or W/mL). 𝑃 = 𝑚𝑐 𝑝 𝑑𝑇 𝑑𝑡 𝑈𝐼 = 4𝑃 𝜋𝐷2, D – diameter of probe(cm) 𝑨𝑬𝑫 = 𝑷 𝒗 , v – volume of medium(𝑐𝑚3)
  • 16.
    Product variables • Volume •Temperature • Viscosity • pH • Soluble solids • Gas concentration Process variables – frequency, amplitude cycle, exposure time & Acoustic energy density.
  • 17.
    Effect on microorganisms •Appropriate ultrasound can promote the growth of microbial cells. • Low intensity ultrasound provides steady cavitation and causes repairable damages. It changes the living state of microbial cells leading to accelerate of their proliferation and more products of metabolism. • High intensity ultrasound can not provide accelerating proliferation effect due to its unrepairable damages. • Resistance to ultrasound in the order of Gram negative bacteria<Gram positive bacteria<Yeast<spores , depend upon their complex structures.
  • 18.
    Inactivation mechanisms • Bacteriacell wall damage, due to mechanical effects induced by pressure gradients generated during the collapse of cavitation bubbles within or near the bacteria. • Shear forces induced by micro-streaming which occurs in the bacterial cell itself. • Chemical attack due to formation of free radicals during cavitation which attack the cell wall structure leading to disintegration. In addition there will be the formation of a small amount of hydrogen peroxide via sonication, which itself is a bactericide.
  • 19.
    • Sonication hasbeen less effective to gram positive bacteria such as Staphylococci aureus and Enterococci due to their tough cell wall structure. • Ultrasound is relatively less effective against spores due to their resistance to damage. • Yeast cells may be resistant to physical effects of ultrasound because they are relatively rigid structure and they are not disrupted by microstreaming.
  • 20.
    Effect on enzymes •Acoustic cavitation induced by ultrasound waves, both physically and chemically affect enzymes. • Denaturation of protein is highly responsible for enzyme inactivation either by free radicals in sonolysis of water molecules or shear forces resulting from the formation or collapse of cavitation bubbles. • Enzymes such as catalase, yeast invertase & pepsin are resistant to ultrasound. • Enzyme inactivation mechanism is complex and depends upon several factors such as fruit juice composition, pH, enzyme type and processing parameters.
  • 21.
    • Enzyme inactivationincreases with increase in solid content and decreases with increase in enzyme concentration. • Decrease in inactivation is observed at high fat food molecules. • Generally, higher enzyme inactivation is reported for probe type systems than ultrasound baths.
  • 22.
    Fruit juice enzymes •Pectinmethylesterase (PME) – hydrolyses pectin results in reduced viscosity. (D-value reduced from 45 min to 0.85 min in tomato juice. Lopez, 1998) • Polyphenoloxidase (PPO) – copper containing enzyme causes enzymatic browning. • Peroxidases (POD) – heme containing enzyme causing off-flavors and browning pigments. Thermally stable. • Lipoxygenase (LOX) – related to oxidation of fatty acids and pigments.
  • 23.
    Dairy enzymes • Sonicationof milk results in a diversity of physicochemical changes in macromolecules including enzyme inactivation, homogenization, reduction in fermentation time during yoghurt preparation and improvement of yoghurt rheological properties. • Heat resistant lipase and protease were destructed (can withstand UHT). • Differences observed in the inactivation of the native milk enzymes such as alkaline phosphatase, γ-glutamyltranspeptidase, lactoperoxidase, whey proteins (α -lactalbumin and β-lactoglobulin) in whole and skim milk due to its composition. • Very less effect of sonication on milk enzymes without high temperature.
  • 25.
    Critical Factors Governing microorganismand/or enzyme inactivation are, • Nature of ultrasonic waves or amplitude • Exposure time • Microorganism or enzyme type • Volume of food to be processed • Composition of food • Temperature
  • 26.
    Application • Application ofultrasound to food processing divided into two categories. - To replace traditional processing techniques. - Ex : food cutting, emulsification/homogenization, pasteurization/sterilization, meat tenderization and degassing, etc. - To assist the traditional techniques. - Ex : extraction, freezing, thawing, oxidation, brining, filtration and drying, etc.
  • 27.
    In diary (PU) -Dueto shear forces – viscosity decreases. -In encaps. Solution containing polymer (protein) is denatured and absorbed on surface Of liq. Droplets & radicals cross links proteins
  • 28.
  • 30.
    Disadvantages • The lackof standardization in ultrasound operating frequencies and power levels makes comparison between different effects were difficult. • Direct contact between probe and food medium. • Effect on color & antioxidants has been reported in some sonicated samples due to degradation of pigments (anthocyanin, ascorbic acid, lycopene & carotenoid) at high energy levels. • However, during emulsification and processing of vegetable oils, a metallic and rancid odor has been detected only for insonated oil and foods.
  • 31.