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E3TE3T EnergyEfficiencyEmerging Technologies
Microwave Assisted ThermalSterilization - MATS™
Emerging Technologies ShowcaseJanuary 21, 2015
Bill Wilson, P.E.
Washington State University Extension EnergyProgram
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Introduction
What we are going to discuss:New process technology for post-packagingprocessing (sterilization) of low-acid/high-moisturefood products resulting in long-term, ambientcondition, shelf-stable, food products preservation
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BPA TI Project Funding Acknowledgement
http://www.bpa.gov/Doing%20Business/TechnologyInnovation/TIPProjectBriefs/2014-TIP-261.pdf
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Microwave Assisted Thermal Sterilization (MATS™)
• Developed by Dr. Juming Tang’s Microwave Group at WashingtonState University, Pullman Campus – affiliated with the Department ofBiological Systems Engineering
• Adaptation of 915 MHz frequency microwave energy for internalheating of food products in their hermetically sealed storagecontainers to sterilization temperatures
E3TE3T EnergyEfficiencyEmerging TechnologiesE3TE3T EnergyEfficiencyEmerging Technologies
• Process for deactivation of microorganisms and their spores.Internal temperatures in excess of 212oF required (generally 250 –265oF), with adequate “holding” time once temperature is reached
• We are all very familiar with conventional post –packagedsterilization technologies as food processors, domestic foodpreservationists, or consumers
• Examples of products created using conventional technologies andtarget categories for MATS™ technology follow ….
What is Post-Packaging Sterilization?
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How is Post Packaging Thermal Sterilization Achieved?
• Imparting thermal energy to heat container andcontents to sterilization temperature
• For flexible or semi-rigid non-metallic containersin particular must be done in pressurizedatmosphere environment to avoid product watercontent vaporization
• Most frequently, pressurized atmosphere is steam(15 psig sat. steam ~247oF), or hot water atsterilization temperature maintained at 20 psig orgreater pressure
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Attributes of MATS™ vs. Conventional Technologies
• Benefits Significant reduction in thermal processing time (1/4 to 1/10 of conventional
processing time) Greatly improved product visual and sensory appeal - particularly prepared meals
containing delicate ingredients Improved nutrient retention Inherently capable of adaptation to continuous-type sequential processing system
design Shelf-stable end-products eliminate refrigeration requirements for processing,
warehousing, transportation, retail sales storage/presentation Initial indication of a reduction in processing energy intensity (gross combined
process energy consumption/unit mass of product) – usually stated as Btu’s per lb.of product
• Drawbacks Processing energy cost/production unit increase due to electrical vs. thermal
energy utilization (particularly for natural gas)
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Conventional Sterilization Methods
• Conventional Technologies
Steam heated retorts (also called “autoclaves”)
Water immersion retorts
Steam water spray retorts
• All types –
Batch operation (most typical)
Continuous operation (rare)
Disadvantages Warm-up losses Vent & bleeder losses Product thermal mass Long come-up & cook
time Long product cooling
time
Batch-Type Retorts – “Still” Steam
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Batch-Type Retorts – Water Immersion(with Water Recovery Vessel)
Disadvantages Warm-up losses Long come-up & cook time Long product cooling time
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Batch-Type Retorts – (Steam Water Spray)
Disadvantages Warm-up losses Electrical & Compressed
Air Consumption
Advantages No Steam Venting Loss No Continuous Bleeder Loss Minimal Water Volume Heat-up
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WSU MATS™ Semi-Continuous 40 kW Pilot Line
View: Preheating Section (lower) MicrowaveSection (Upper)
20 KW 915 MHz MicrowaveGenerators
Summary of WSU MATS™ Major Milestones
July 2001 Formed WSU Microwave Consortium I
July 2001 Developed first 915 MHz single mode pilot system (10 kW)
Oct. 2006 Received US patent for 915 MHz single mode microwavesterilization system design
Aug. 2007 Developed a second generation system semi-continuoussystem (40 kW)
Oct. 2009 Received FDA acceptance for MW sterilization of mashedpotato in 10 oz. trays
Nov. 2010 Formed MW Consortium II, focusing on commercialization
Nov. 2010Food Chain Safety (Maple, Valley, WA) is granted license forexclusive rights for commercialization of MATS™Technology [Now 915 Labs]
Dec. 2010 Received FDA acceptance for MWsterilization of salmon fillets in sauce in 8 oz. pouches
Mar. 2012 Received non-objection letters from USDA FSIS
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Retort Processes Energy ConsumptionComparisons
• Like many Energy ConsumptionComparisons – “It Depends” Currently batch or continuous
operation?
Product temperature increase required
Equipment capacity utilization anddensity of product pack
Initial projection of Microwave comparedwith batch processing indicatesfavorable energy intensity and overallenergy efficiency metrics
EnergyIntensity??
Commercial Assessment Outcome Summary
7.110.4
32.5
0
5
10
15
20
25
30
35
Still Steam Immersion w/ WaterRecovery
Steam Water Spray
Lb/F
t3
Lb. Product/Ft3 Usable Retort Volume(As Measured/Estimated) Product/Volume
Ratio
864
1,293
300 260
0
200
400
600
800
1,000
1,200
1,400
Still Steam Immersion w/Water Recovery
Steam WaterSpray
ContinuousRotary Retort
(cans)
Ener
gy In
tens
ity, B
tu/l
b Pr
oduc
t
Energy Intensity(As Measured/Estimated)
Energy Intensity
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Commercial Assessment Outcome Summary
651
1293
658
260
0
200
400
600
800
1,000
1,200
1,400
Still Steam Immersion w/Water Recovery
Steam WaterSpray
ContinuousRotary Retort
(cans)
Ener
gy In
tens
ity, B
tu/l
b Pr
oduc
tEnergy Intensity
Normalized for Pack Density & Temp. RiseEnergy Intensity
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Input Energy Distribution
29.0% 18%
56.2%79.2%
0%
10%
20%
30%
40%
50%
60%
70%
80%
90%
100%
Still SteamHorizontal
WaterImmersion
Steam WaterSpray
ContinuousRotary
Retort (cans)
Input Energy Distribution(As Measured/Estimated)
Electrical
Product & ContainerSensible Heat:Surface Losses
Preheating
Bleeder Losses
Vent Losses
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WSU Microwave Group: www.microwaveheating.wsu.edu
Food Chain Safety/915 Labs: www.fcsmats.com
Bill Wilson: [email protected](360) 956-2041
For Additional Information:
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