ATTACHMENT C - CRITICAL REVIEW

This section reviews work accomplished toward meeting the objectives ofNC-136 during the five-year period 1995-2000. The scope of the scientific output is
indicated by the five-year list of peer-reviewed publications from participating stations, found at the end of this review. The Critical Review will emphasize work and
its impact, resulting from the cooperative efforts of the participating scientists.

Major accomplishments The sharing of ideas, approaches, results and critical reviews was the single most important accomplishment of the project. Annual
meetings for the project presented a forum for collective discussion involving the largest group of researchers in the U.S. interested in advancing thermal processing
of foods. The format of annual meetings allowed detailed presentation of collaborative and other research efforts to the entire group. This provides a critical review
of the research on an ongoing basis. Critical and constructive comments continue beyond the duration of presentation and often lead to new and enhanced
collaborations. Members often commented that NC-136 is one of the most important professional meetings that they attend.

Table Cl. Major accomplishments of NC-136, 1995-99
   Number (multistation)
Journal articles, peer reviewed  520 (17)
Books and book chapters  102 (7) 
Presentations  320 (8)
Theses and dissertations   92
Patents 15
 USDA NRI grants  $1.75 million
 Other competitive grants Over $16 million

Major accomplishments are summarized in the Table Cl above. The large number of peer- reviewed publications speaks for the quality of science. The depth and
breadth of the work mentioned below show that the participating stations are strongly committed to NC136. For a number of stations, the small financial support
from the NC136 project was used as seed money to leverage external funding in a very impressive way from industry and governmental agencies, as shown in Table
Cl. In the case of one station, the station representative thought that the leverage has been at least five-fold.

Impact

The project has contributed greatly to the development of food thermal processes based on sound fundamental principles. Detailed impact statements can be found
following accomplishments in each of the research topics described under the three objectives. Collaborations of multiple stations in several ad-hoc committees on
rheological properties of foods and their measurement techniques have led to development of standard measurement procedures. Such standard methods reduce
operator and instrument variability and provide more accurate data for product and process design. NC-136 made such collaboration possible. In phase transitions
in foods, collaboration has led to an IFT Basic Symposium as well as an authoritative book on the subject, in addition to scientific accomplishments. Thermal analysis
using the DSC was standardized by a six station-subcommittee so that more accurate data can be obtained in the difficult measurement process of glass transition.
An authoritative reference book on microwave processing of foods is being published as a result of collaboration between stations. Guidelines for aseptic processing
were developed in a workshop organized by several of the stations by obtaining people from academia, industry and government. Development of a new process of
microwave sterilization that ensures food safety while improving product quality benefited significantly from collaboration between NC-136 stations. Validation of
commercial sterilization to ensure food safety requires critical kinetic parameters that were developed through collaborative studies between stations. The sharing of
information and the cooperation fostered by NC 136 were directly responsible in initiating and carrying out these important tasks relative to food research.

Dissemination of information
Information generated in this project was made available to others through the 320 presentations at national meetings and 354 publications in widely-read scientific
journals, plus reference books, development of several short courses and a website specifically developed for NC136. Two short courses, one on aseptic
processing and one on the emerging processing technologies were developed through collaboration of a number of stations. These workshops were very well
attended by personnel from food processing and equipment industry, government and academia. Two symposia were developed for Annual IFT meetings that attract
the largest audience from food industry and academia. Impact to education has also been very significant as the cutting edge research in quality and safety of food
processing was included in graduate and undergraduate courses taught at the participating stations.

Although the accomplishments of NC-136 have been impressive, continued cooperative work in many areas is critical. Consumer convenience and safety,
preference for healthier and tastier foods, and the use of new food processing technologies mandate continued research. Our proposed objectives for the next five
years are slightly modified to reflect this goal. The remaining section is organized in terms of the three objectives of the completed project with the accomplishments
and the continued needs for research discussed under each subtopic.

OBJECTIVE A:
To Identify and Quantify Important Physical and Biochemical Properties of Thermally Processed Foods and Factors Affecting These Properties

Al. Rheological Properties. Rheological (deformation and flow) properties of foods strongly influence food quality, safety and the design of processing and handling systems. Studies include rheology of fluid and semi- solid foods, development of improved measurement techniques, mathematical modeling of material behavior, and rheology for process design.

Al.l Improved Measurement Techniques. The Yield Stress Subcommittee consisted of numerous stations (IA, MI, MO, NY-Geneva, ND, OH, PA) over
several years of the project. During the course of this study, each station developed the capabilities to measure the yield stress of fluid and semi-solid foods using the
vane method. Identical products (applesauce, ketchup, and chocolate) were tested by each station using carefully defined methodology. The subcommittee met
every year to discuss previous results and plan subsequent trials. Working within the infrastructure provided by NC-136, the group was able to achieve the primary
objectives of the subcommittee: 1) to establish the controlled rate vane method as a standard procedure for measuring yield stress, and 2) to establish standard
terminology (static versus dynamic yield stress) to describe the time- dependent nature of the phenomenon. The new procedure has wide applications in the food
industry.

A Brookfield Viscometer equipped with a small sample adapter (18 ml) and a flag impeller was used to evaluate the average shear rates of mixing processes (Briggs
and Steffe, 1996). A shear rate value of 2.92 /rad is recommended for routine work. Results were compared to those from a controlled stress rheometer and
excellent agreement was found. This system provides a useful, low cost, means of testing power law fluids. Mitschka's method* to convert Brookfield instrument
readings into viscosity values was evaluated using disc-type spindles (Briggs and Steffe, 1997), and found to be acceptable for many fluid foods. Also, a vane tester
was designed and constructed to measure the yield stress of ice cream at typical scooping temperatures of-12°C to -16°C (Briggs et al., 1996). Yield stresses from
2.5 to 8.0 kPa were observed. This technique makes it possible to objectively evaluate reduced fat ice cream formulations.

A direct-drive concentric cylinder viscometer in a pressure chamber was used to study the flow behavior of a 11 °Brix tomato puree over the temperature range : 76
to 120 °C, and the apparent viscosity versus temperature profiles of a 4.0% waxy rice starch dispersion during continuous heating from 30 to 110 °C (Rao et al.,
1999).

Future Needs: Rheological methods need to be developed for many foods including nonhomogeneous fluids and foams.

A1.2 Studies on Fluid and Semi-solid Foods Rheological properties of fluid and semi-solid foods are being characterized at the MI, NC, NY- Geneva, and WA
stations. They have dealt with understanding the role of composition on the properties and measurement techniques. In a collaborative study between the MI and
NY- Geneva stations, measurement of yield stress using the vane method and the role of yield stress in suspending solid foods were reviewed (Rao and Steffe,
1997). This helped develop "state-of- the-art" methodology for other stations.

Rheology of wheat dough was studied in terms of the influence of energy level, type of deformation (shear versus extensional) and strain history on dough
development (Campos et al., 1997). Results indicate a strong correlation between the degree of deformation and the development of protein structure in wheat
dough. These results may lead to significant improvements in the process and product development in the baking industry.

Various starches, proteins and their combinations were studied to identify the effects of interaction between the components and temperature on their rheology.
Rheological studies on cornstarch and waxy maize dispersions showed that the consistency index of the dispersions increased exponentially with mean granule
diameter (Okechukwu and Rao, 1995; 1996). Starch granules also played an important role in the rheology of mixed wheat starch-gluten pastes (Champenois et al.,
1998) and waxy maize starch dispersions (Chamberlain et al., 1999). Such data are important for designing a number of thermal processes.

Dynamic rheological data revealed weak gel-like behavior of both 10% corn starch and soy protein isolate (SP) dispersions; the storage modulus of cornstarch
dispersion was higher than that of SP isolate. Plots of protein/starch ratio vs. storage modulus revealed phase separation and inversion (Chen et al., 1996; Liao et al.,
1996). In protein and starch gels (cowpea protein and 10% solids cowpea starch), the modulus increased due to aging and starch concentration. These results led to
important product improvements by increasing our understanding of ingredient functionality.

The studies of Champenois et al. (1998) improved our understanding of starch and gluten interactions in starch pastes. The addition of gluten changed considerably
the viscoelastic properties of starch pastes. In starch dispersions, the rheological unit was a starch granule. When gluten was present, the rheological units were the
"cells" formed by gluten fibrils and filled by starch granules. The internal lipids in flour played an important role so that flour is not a simple blend of starch and gluten.
Results lead to improvements in the texture of bakery products.

Viscosity of a starch dispersion as a function of temperature and shear rate during gelatinization are found in the temperature range 60-95°C (Yang and Rao, 1998;
Lao et al., 1999). These data are needed, for example, in establishing the safety of thermal sterilization of foods containing starch.

Electrorheology (ER) is the area of rheology that evaluates changes in material flow properties during exposure to electric fields. Applications of this technology in the
food industry may unleash new techniques for traditional processing, and was studied for chocolate. The voltage altered the rheological behavior of the fluid - voltage
polarized particles prompting structure formation in the fluid, leading to a greater resistance to flow. In the absence of an electric field, practically all fluids exhibit a
decrease in the apparent viscosity at higher temperatures. The opposite response described here is typical of the unusual behavior found in ER fluids (Daubert and
Steffe, 1996). A prediction equation was developed that allows prediction of chocolate viscosity during exposure to electric fields, and delivers a means of selecting
and controlling milk chocolate viscosity with voltage (Daubert et al., 1998). Much work, however, still remains to harness this technology in the form of food
processing applications. The chocolate industry may benefit from this technology by externally controlling the flow properties of milk chocolate, allowing the
development of new processes and products.

Future work: Due to the complex nature of foods, much more work needs to be conducted in order to understand the role of composition and their interactions on
the viscous and viscoelastic properties. As a first step, work on food polymers should help our understanding of the role of macro and microstructures, and
rheological elements on food rheology.

A1.3 Rheological Properties During Various Processes Measurement of the rheological properties of fried product and frying medium as an important aspect
of food frying research. One of the most important quality attributes of a fried product is its crispness. Development of texture the during frying process was studied
(Fan et al., 1997; Pinthus et al., 1998; Normen et al., 1998; Rovedo et al., 1999). The influence of various components of starch and post-frying moisture migration
on the texture and other mechanical properties of fried products was studied. Force-deformation studies have been performed by several researchers to predict
texture of fried products such as French fries and tortilla chips. In general, a fried product becomes tougher as frying time increases up to an optimum value after
which the product becomes brittle. Porosity and pore size distribution, important for texture and oil absorption, were evaluated at the TX station. Changes in oil
viscosity due to degradation and temperature changes during a frying process, with major implications in the rate of heat, moisture and oil transfer were also studied
at the CA and TX stations. Based partially on these studies, an optical sensor for monitoring changes in oil quality has been developed for use in industry.

Future Needs: Although considerable progress has been made in the measurement and understanding of physical properties of the oil and food product during
frying, there is still work needed to improve textural quality and reduce oil absorption in frying. There is lack of data on critical properties such as permeability of
porous food materials. A method to determine the surface tension, between the oil and the product, needs to be developed so that the effect of oil degradation and
surface interaction during the process can be better described.

A2. Phase Transitions in Foods During heating and cooling of foods, there are many phase transitions that may change the physical properties of the material.
These transitions are important in a wide range of food products, including frozen foods, confectionery products, cereals, milk powders, and many starch-based
foods. It is important to understand these phase transitions and to be able to control them so the desired attributes are obtained in the product. Many components of
foods undergo phase transitions (i.e., ice freezing, starch gelatinization, glass transition, crystallization of sugars and lipids, etc.), and research in this area by NC-136
members (led by NY-Geneva and WI) has led to publication of a book on the topic of Phase/State Transitions in Foods.

Cooperative research headed by the OR, WI, and IA stations, with contributions from 6 other stations (MN, MO, NE, NJ, ND, OH) on a round robin differential
scanning calorimetry thermal analysis study to determine onset and peak transition temperatures and enthalpy was completed (Kolbe et al., 1998). The
reproducibility of these measures using three types of commercial equipment for both starch gelatinization and tristearin melting and crystallization was determined. he
transition temperatures and enthalpy values for starch were similar among laboratories, as were the melting and crystallization temperatures for tristearin. Enthalpy
values for tristearin were consistent among most laboratories, but significant differences existed between DSC types. Based upon the findings of the cooperative
study, instrument usage and laboratory conditions play a major role in determining transition temperatures and enthalpy values. Interdependent station activities may
prove useful for determining expected errors in other DSC measurements, and the evaluation of new calibration materials. This research will be continued with further
collaboration between the OH, WI, NE and IA stations. Additional standardization of enthalpy measurements and the standardization of the procedure to determine
the glass transition temperature of water in different food systems will be investigated.

The effects of various operating parameters on the kinetics of crystallization (sugars, lipids, and ice) have been measured for different foods. For example, the
changes in ice crystals during storage and distribution of ice cream were modeled based on previously determined kinetic parameters. The effects of temperature and
extent of temperature fluctuations on recrystallization kinetics were determined (Donhowe and Hartel, 1996) and then used to model changes during normal shelf life
conditions (Ben-Yoseph and Hartel, 1999). These results clearly show the beneficial effects of maintaining low temperatures during the early stages of storage in the
process plant. Study on the effects of processing parameters on crystallization of lipids showed that depending on process conditions, foods with different mechanical
properties could be produced simply by altering the lipid crystalline structure (Hen-era and Hartel, 1999a and b). By understanding the relationships between
crystallization conditions and structural properties, we can control the mechanical properties of lipid-based food products.

There is increasing evidence suggesting a unique relationship between the glass transition temperature of a food and the rate of quality change during the storage of
low moisture and frozen foods. Effects of glass transitions on shelf life and quality in low moisture and frozen foods are being investigated at MN, MO, NJ, and OH
stations.

Structure development rates in a gel, its melting temperature, and enthalpy of melting were studied as a function of composition. For example, high-methoxyl
pectin-Na alginate-fructose (65%) showed a stronger dependence on Na alginate content than on sugar or pectin content (Rao and Cooley, 1995). Physical gels
develop slowly and structure development rates provide quantitative information. These data should be useful in scheduling gel-production. While the enthalpy of
melting of sucrose gels was higher than those of plain gels, that of sorbitol gels was lower, reflecting the important role of the hydroxyl groups in the sugars (Fu and
Rao, 1999). Gel melting temperatures were also studied that should be useful in selecting ingredients, such as pectins, and in developing gels with a specific melting
temperature.

Several methods are currently available for measuring the glass transition temperature of a food including DSC, DMA (Dynamic Mechanical Analysis), and TMA
(Thermal and Mechanical Analysis), etc. The results often differ from each other due to differences in the testing methods as well as testing procedures such as
heating rate or frequency. Our DSC ad-hoc committee has started to develop a protocol for measurement and analysis of the glass transition temperature using
DSC. This protocol should reduce instrument and operator dependence of the data and make it more consistent and reliable for design of products and processes.

Future Work: Our understanding of phase transitions during heating and cooling of foods is still severely lacking due to the complexity of most foods. The
interactions between components in real foods make extrapolation of results from pure, model systems very difficult. It is the effects of these complex interactions
that will be the focus of most future work in this area. Most of the glass transition temperatures reported in the literature so far are limited to classical single-phase
food products. Data on multi-phase food products are needed for the food industry to develop new and innovative food products.

A3. Colloidal and Interfacial Properties of Foods Colloidal constituents affect and determine the behavior of many foods, including milk, ice cream, butter,
mayonnaise, and cheese, all of which derive their characteristic properties from the fact that they are colloids. As a result, colloid and interface science provides a
microscopic framework for understanding and characterizing many macroscopic food behaviors, including bulk rheological behavior, and structural integrity of
emulsions and foams. For example, the adsorption, distribution and/or interactions of proteins and surfactants at the liquid-liquid interface determine the behavior of
all food emulsions and microemulsions. This, in turn, determines such properties as shelf life and foam stability. An important advantage of colloid and interface
science is that its fundamental principles can be used to study materials that appear to be disparate. Therefore, lessons and techniques from other fields of study can
be used to benefit food systems. This provides a powerful tool that enables one to a gain molecular-level understanding of macroscopic food behavior.

Work done at the MI Station so far has focused on the adsorption and interactions of proteins at the oil-water interface. The recent development of a total internal
reflection fluorescence microscopy technique has allowed for quantitative molecular-level investigations of macromolecular adsorption and interactions at liquid-liquid
interfaces. This apparatus, coupled with fluorescence photobleaching recovery (FPR), has been used to qualitatively establish the relative importance of bulk and
surface diffusion of representative proteins at the oil-water interface. We have developed a procedure for calculating interfacial protein concentrations on the basis of
fluorescent emission data, and studied the effect of extrinsic fluorescent labels on the adsorption and diffusion of proteins.

Future Work: Work in the upcoming funding cycle will focus on the interactions of various food proteins and commonly used surfactants at the oil-water interface.
In particular we will investigate the competitive adsorption of a-casein and b-casein (the two major milk proteins) in the presence of surfactants such as the tweens.
We will seek collaboration with other stations on how the interfacial adsorption/interactions of various food proteins and surfactants affect the uptake and/or delivery
of selected nutrients and vitamins. This is a major undertaking that should be of a great deal of interest to the food industry, and will benefit from current collaborative
work with the OR station in which we are exploring the efficacy of using proteins as drug delivery instruments.

A4. Electrical Properties of Foods

A4.1 Dielectric Properties of Foods for Microwave and Pulsed Electric Field (PEF) Processing. For the food industry and the consumer to benefit from the
convenience of microwave heating knowledge of dielectric properties and how they change during processing are critical. Studies on dielectric properties are being
conducted at the OH, PA and NY-Ithaca stations. Collaborative work between OH and NY-Ithaca was presented in the 1997 Conference on Food Engineering.

Dielectric properties of foods were measured in the range from 0 to 130 °C for the first time which is important for microwave food sterilization processes. Phase
changes, such as starch gelatuzation and protein denaturation during heating, changes the dielectric properties that have implication in the sterilization process.
Changes in dielectric properties of cheese as a function of storage time showed significant changes, of implication to microwave heating of pizza and other cheese
containing products. Some of these studies are part of a larger collaboration between the stations and other agencies (U.S. Army Natick Laboratories) to determine
the dielectric properties at sterilization temperatures, and use this information in better understanding microwave sterilization. Microwave sterilization is being used in
Europe to produce high quality commercially available meals - such technology can improve the quality of foods for our consumers and soldiers in combat and make
it possible to export high value commodities.

Dielectric strength is the magnitude of electric field at which the insulating properties breakdown and there is a discharge. Systematic data on dielectric strength of
various food products are needed for design of ohmic heating and pulsed electric field processing that can improve the quality of processed food significantly.
Dielectric strength of various liquid foods with small size air bubbles were determined (WA). Air bubbles break down in liquid foods at an electric field of 22 to 25
kV/cm. De-aerated samples were able to withstand more than 80 kV/cm of electric field without breakdown. Pressurization of the food increases the dielectric
strength of foods and makes it possible to allow the application of PEF technology (OH) in some situations Without such critical information, novel technology (such
as PEF) for improved food quality cannot be implemented.

Future work: Future needs are to measure the dielectric properties at sterilization temperatures for a wide range of food items, understand the changes in the food
that contribute to changes in dielectric properties and develop accurate predictive models at these temperatures. Dielectric properties of frozen and partially frozen
foods are needed. Such data will provide understanding of how the dielectric property changes during the freezing/thawing process, which is necessary for designing
products such as frozen microwaveable dinners.

A4.2 Electrical Conductivity of Foods for Ohmic and PEF Processing Electrical conductivity information required for the design of ohmic heaters for aseptic
processing has been measured and empirically modeled for various model solutions and multiphase foods such as beef stew (OH and NCFST stations). Electrical
conductivity has also been measured in the context of pulsed electric field (PEF) processing (WA). In general, the electric conductivity measured in a high voltage
pulse field is 10 to 20% higher than that measured with a DC type electrical conductivity meter. This is attributed to electrolysis during DC type measurements and
temperature increase of the sample under high voltage PEF measurements. Electrical conductivity of liquid foods for a range of processing temperatures have been
accomplished for low pulse field which are in good agreement with high pulse field (OH). A database is being established for the design of electro technology based
food processes (OH).

A5. Kinetics Collaborative work between FL and NC stations has continued to evaluate the performance of two alternative techniques for the determination of
kinetic parameters under dynamic temperature conditions (Moody, 1997). These kinetics provide the engineering parameters upon which the design and validation
of commercial sterilization and pasteurization processes are based in the food industry.

Bacterial and enzyme kinetics are needed for development of new pasteurization processes. Kinetics of microbial load and trypsin inhibitor in soymilk were studied
by the IA and ND stations. They demonstrated that times and temperatures greater than those required for the pasteurization of cows milk are required for soymilk.
Coagulation kinetics of soymilk to manufacture tofu were studied to develop methods to monitor coagulation in the manufacture of torn. The influences of processing
method, protein composition, soybean variety, and whole vs. flaked soybeans on the yield and composition of torn were reported by both stations (Moizuddin et al.,
1998; 1999). All of these studies have improved the thermal processing of soybeans into soyfoods. Industries are currently utilizing these findings to improve the
quality and safety of their products. Based upon these studies a new reduced-fat tofu was introduced into the marketplace.

Kinetics of several microbiological changes were studied, with implications to food safety. These included Salmonella dublin exposed to pulsed electric field,
thermal destruction of E. coli 0157:H7 in a slaughterhouse operation, Listeria monocyotgenes Scott A. in milk under conventional and microwave heating, and
Fusarium mold growth during barley making. Kinetics of several biochemical changes were studied, with applications to new product and process development.
These included degradation of capsaicin or spice heat (Roche-Herrera and Wilson, 1999), formations of pyrazines (aroma/flavor) during Maillard reaction,
degradation of chlorophyll in pureed green peas, retention of flavor during extrusion, and contribution of chlorination in cake-baking.

Future Work: Kinetic data is still needed for the improvement and development of thermal and alternative processes. The influence of the glass transition
temperature on these processes and products needs to be investigated using reliable methods (DSC Ad-hoc Committee is looking into this). This includes the
determination of kinetics associated with microbiological, enzymatic, chemical, safety and quality changes. This data will be used by multiple stations to design and
validate methods for the commercial processing of foods that are safe and nutritious, with high consumer acceptance (sensory properties). Multi-station collaboration
will continue in this area.

OBJECTIVE B:
To Identify And Describe Mechanisms For Heat, Mass, And Momentum Transfer In Thermally Processes Foods And The Extent To Which They
Are Affected And Governed By Parameters Covered By Objective A

Bl. Aseptic Processing of Fluid Foods and Particulates Aseptic processing can provide much improved food quality and more efficient industrial processing.
Aseptic processing has entered the mainstream as an industry practice for fluids, but its application to particulates is currently limited. Aseptic processing of
particulates has been widely investigated over the past fifteen years. A NCFST-CAPPS (National Center for Food Safety and Technology and Center for
Advanced Processing and Packaging Studies) workshop, co-sponsored by several of the NC-136 participating stations and with participants from several other
NC-136 institutions, has been termed "historic" in terms of defining the safety considerations required (Damiano, 1997; Degeronimo et al., 1997; Larkin, 1997;
Marcy, 1997; Sastry, 1997). Discussions during the workshop have subsequently resulted in a successful process filing by Tetra Pak. However, there has been no
major attempt by companies to file a process since that time.

Industry reluctance to file processes may be attributed in part to caution, partly to the extensive filing requirements, or a lack of significant quality advantages for the
technology if all the safety issues are addressed to the satisfaction of the Food and Drug Administration. Consequently, it is still necessary to improve the safety of
processes further while not sacrificing quality; i.e. a major effort in optimization is necessary. In addition, the advent of nonthermal process technologies has
introduced a new dimension of complexity to the task.

In the area of particulate-fluid flow, studies have ranged from applied work on residence time distribution to a number of fundamental studies aimed at modeling
solid-liquid flows (Liu and Zuritz, 1995; Hu, 1996; Lareo et al., 1997; Unluturk et al., 1999). While these are useful in characterizing average flow outcomes for
mixtures, the prediction of real food flows with large particle loadings has remained elusive.

Estimation of solid-liquid heat transfer coefficient is in the heart of developing aseptic processing of particulate foods. Various measurement techniques have been
developed to determine realistic values of heat transfer coefficients (Barigou et al., 1998) needed for development of microbiologically safe processes. Alternative
methods of heating such as ohmic and radio frequency continue to be investigated (Orangi et al., 1998; Sastry and Salengke, 1998).

Future Work: While fluid processing is now routine, a major opportunity exists to reduce process requirements by applying thermal and nonthermal processes
individually or in combination to produce high quality liquid products. The kinetics of such processes are yet to be investigated, although IFT is conducting a study for
FDA on the kinetics of alternate process technologies. Future improvements in the technology will not only need to deal with safety assurance, but also improve
product quality significantly, as with internal generation (ohmic, radio frequency and microwave heating) and nonthermal processes. Convective heat transfer
coefficient between solid particles and fluid show a wide variation between laboratories, indicating the need to develop comparable methodologies. Effects of various
processing parameters when using internal heat generation would need to be investigated. Fouling of heat exchange surfaces with proteinaceous foods still needs
development, as evidenced by a recent issue of the Transactions of the Institution of Chemical Engineers devoted entirely to the subject (Dun- and Grasshoff, 1999;
Gillham et al., 1999; Robbins et al., 1999).

B2. Microwave Heating Making food products microwaveable is still one of the top aspirations in the U.S. food industry. Another area of industrial importance is
the use of microwaves in processes such as sterilization for improved quality. Heat and moisture transfer associated with microwave heating of food can have a
major impact on the final quality of foods.

Collaborative work between PA and NY-Ithaca stations has led to a comprehensive book on microwave processing of food (Datta and Anantheswaran, 2000). It
is the most complete collection of information for the U.S. food industry in developing innovative microwave food products and processes. Collaboration between
OH and NY-Ithaca station has also been useful in developing a Symposium on Microwave Food Sterilization during the IFT 2000 Annual Meeting.

Heating non-uniformity of microwaves due to product and equipment variables are of great significance. Accurate models of heating non-uniformity were developed
by coupling the electromagnetics and heat transfer and validating the results using chemical marker formation. Only through such coupling was it possible to
demonstrate how the cold point in a sterilization process changes during the heating, with major implication to safety of such processes. Enhanced heating (focusing)
in certain food shapes and properties, that lead to unusual (compared with conventional) heating and moisture transport were identified (Zhang and Datta, 1999).
These provide guidelines for all product and process development, although application to differential heating of food components in a multi-compartment frozen
dinner was studied in detail. Microwave pasteurization of shell eggs without major protein denaturation was studied in the Illinois station (Sullivan and Padua, 1999).

Understanding moisture transport in microwave heating should lead to reduction of sogginess and over-drying of foods heated in microwaves. Experimental moisture
profiles as affected by heating parameters were studied (Zhou et al., 1995; Lin et al., 1995). Heat and mass transfer coefficients, important for quantitative
understanding of heat and moisture transfer was measured (Mukherjee et al., 1997). A comprehensive multiphase porous media transport model (Ni et al., 1999)
identified the various modes of moisture transport, such as capillarity and pressure driven ' flow. Pressure gradients in the microwaved food due to internal heating
and vaporization significantly enhance the moisture transport making the food surface soggy and increasing the moisture loss.

Infrared and hot air-assisted microwave heating of food to reduce surface sogginess of microwaved foods was studied (Datta and Ni, 1999). When absorbed
mostly on the surface, infrared can reduce surface moisture and, beyond a threshold power level, it can reduce the' surface moisture to lower than its initial value. Hot
air also can reduce surface moisture and increase surface temperature, but not as effectively as infrared heat. These findings are important for designing products and
processes for combination microwave/ infrared/ hot air heating as they have begun to appear in domestic microwave ovens.

B3. Frying Reduction of oil pickup by fried foods while achieving the right texture and flavor is of considerable interest to the U.S. food industry and consumers. To
achieve this objective will require the understanding of heat transfer, moisture evaporation, moisture movement in liquid and vapor phase and oil pickup during frying.

Convective heat transfer coefficient measures the rate of heat transfer from the oil to the food product and has a major influence on all aspects of the frying process.
The rapid boiling at the surface of food makes this convective heat transfer a complex process. The convective heat transfer coefficient was measured (CA, NC,
OH, and TX Stations) using the lumped parameter approach. These measurements permit a better understanding of the heat transfer mechanism at the food surface
during frying.

The convective heat transfer coefficient decreases as the oil degrades during frying and the coefficient increases with oil temperature. Mass transfer during frying
consists of moisture loss and oil absorption. Moisture loss in chips (tortilla chips) was found to decrease exponentially with frying time. Oil absorption is a complex
phenomenon. Studies on tortilla chips at the TX station suggest that most of the oil does not penetrate the product during frying, but during the cooling period when
the product is removed from the fryer. Detailed experimentation was developed to identify the relative amounts of oil pickup on the surface and inside the food
material.

Future Needs: Work is still needed in better characterization of energy, moisture and oil movements in the product during continuous frying or batch frying. The
effects of water evaporation and the shrinkage of food matrix on the oil absorption have not been understood.

B4. Extrusion Extrusion is an extremely useful but a complex process to the food industry, involving heat transfer, moisture transfer, rheology and kinetics. Studies
on extrusion of foods benefit development of new and value-added products, including alternative non-food uses of agricultural material. Constitutive models and
equations are being applied to analyze the rheo logical behavior and flow patterns in extruders during extrusion of corn meal, corn starches, and wheat starches at
MN, MO, NJ, and TX stations (Zhang and Bhattacharya, 1996; Tsue - Er et al, 1998). In addition, MO and TX stations are also developing adaptive control and
generalized predictive control (GPC) schemes for food extruders (Tsue - Er et al., 1998; Xie, 1999). IL and MO stations are studying the influence of raw material
characteristics, such as particle size and genetics on extrusion processing efficiency (Garber et al., 1997; Faller et al., 1995).

Future needs: A more systematic approach to food extrusion is needed so that the results are easier for scale-up and more transferable from one model of extruder
to another model or from one screw configuration to another screw configuration. Elucidation of changes in the rheo logical behavior of dough in the extruder and at
the die region and their relationship with mechanisms of bubble formation, extrudate expansion, and final extrudate texture were studied. A robust, adaptive,
multi-input and multi-output, and easy-to-implement food extruder controller needs to be developed. A better understanding of the impact of raw material
characteristics on extrusion process efficiency is needed.

B5. Drying Superheated steam impingement drying is a novel technology with potential for food applications. It has advantages such as higher efficiency and
reduced oxidation, and was studied at the TX station. Under the same conditions, superheated steam drying showed a shorter plateau than air drying of corn tortillas.
The effect of temperature and airflow rate on the drying rate and product quality attributes (porosity, shrinkage, texture, degree of gelatinization) were studied.
Tortilla dries faster and becomes more porous at higher temperature but shrinks more at low airflow rates. These studies will allow optimization of this novel drying
process with potential to produce food products with better texture, less quality loss, and increased speed of drying.

B6. Baking The important food process of baking had not been understood quantitatively. Heat and mass transfer in a slab of potato during baking were explained
using a multiphase porous media model (Ni and Datta, 1999). Baking time reduces significantly with thickness, however at a slower rate compared to
conduction-only heating. In addition, the surface temperature also reaches a higher value for a thinner material, which may help develop the often desired crusty
surface. The skin layer formed during baking can reduce the vapor loss from the surface, and consequently increase the surface temperature and center temperature
so that the baking time can be reduced. Decreasing initial moisture content in the food and increasing air temperature and the heat transfer coefficient reduces baking
time. This information would be valuable for the design and optimization of industrial baking processes. Baking of tortillas is being investigated at IN and TX stations.

B7. Modified Atmosphere Packaging (MAP) MAP for fresh produce involves packaging with a gas-permeable polymeric film to obtain a self-generated change
in the gaseous composition in the package. The exact composition of the gas in the package is a dynamic function of the product respiration rate and oxygen
transmission rate through the package and can be achieved by selecting a polymeric film with the appropriate permeability and the amount of produce in the
package. The optimum 0 2 concentration for mushrooms was found to be 6% by the PA station (Roy et al., 1995a). They also noted the need to maintain a constant
temperature (reduce temperature abuse) of the package to maintain the desired gas concentration within the package. This could potentially lead to food safety
concerns since a minimum of 5% 0 2 needs to be maintained within the mushroom package to prevent the growth of anaerobic bacteria such as C. botulinum.
Modified humidity packaging, which does not have the associated risks of growth in C. botulinum with temperature abuse, can improve the present shelf life of retail
mushrooms (Roy et al., 1995b). Suitability of newly developed microperforated films was also studied (Ghosh, 1998). These findings are paving ground for the
introduction of new packaging methods and films for the industry to improve the shelf life of fresh mushrooms. IL station is investigating the ability of corn proteins to
act as gas permeable polymeric film in MAP and storage of fresh broccoli (Rakotonirainy, 1999). MAP technologies for MRE products for the military were
developed by the NCFST and NJ stations, in collaboration with industry and US Army Laboratories at Natick.

Future needs: Microperforated films can be effectively used to develop a modified humidity package for fresh produce to increase its shelf life. There is a need to
develop measurement techniques to monitor water vapor transmission ratio (WVTR) of microperforated films, and to develop models to predict WVTR as a
function of size and number of perforations.

B8. Use of Magnetic Resonance Imaging to Fluid Flow, Heat Transfer and Mass Transfer The advantage of using magnetic resonance imaging (MRI)
compared to traditional experimental methods is that MRI provides spatially localized information as compared to an average over the entire sample. Information is
also obtained non-invasively and hence does not disturb the process. This permits new insight into the dynamics of heat, mass and momentum transfer in foods during
processing, needed for product and process development. Significant results using MRI to study thermal processing include: (1) the measurement of velocity profiles
of non-Newtonian fluids in extruders; (2) simultaneous measurement of velocity and concentration profiles in tube flow and in a scraped surface heat exchanger; (3)
measurement of experimental data to develop a relationship between flow behavior and strain history. Results are used to develop new process control sensors that
maintain product quality and minimize production cost, and to improve equipment design for promoting improved/uniform heat transfer.

OBJECTIVE C: To Develop Mathematical Models, Based on Objectives A and/or B, For the Analysis, Design, and Improvement of Thermal
Processes.
Cl. Frying
A mathematical model based on fundamental physical principles will make the frying process more predictable as a function of various operating
parameters. Such a model will help design better product, process and equipment with less trial and error. This should lead to more predictable final product quality,
improved process efficiency, reduced waste, more accurate control, and microbiologically safer fried foods.

Mathematical models of frying, based on fundamental principles, were developed by the California, NY-Ithaca, and TX stations. Models developed at the CA and
NY-Ithaca stations apply to the frying of a single chip. California station divided the material into wet and dry (crust) regions and was able to predict temperatures,
moisture loss and crust development during frying. NY-Ithaca station applied a more rigorous model by treating the food as a porous media and considering
movement of heat, water, vapor and oil separately by the mechanisms of diffusion, capillarity and pressure driven (Darcy) flow (Ni and Datta, 1998). This showed
the relative importance of the three modes of transport in various regions of the food during the frying process. A heat and mass transfer model developed at the TX
station applied to a batch of tortilla chips and it predicted oil temperature changes during such heating. Another observational model predicted the dynamics of a
continuous fryer and was used to develop a controller for process. Impact of this has been a quantum leap in the understanding of the frying process that is used to
improve product quality, reduce oil pickup and optimize the process. Computer-aided models of frying has been made available to the industry for commercial
applications (CA).

Future Needs: Work in deep-fat frying is still under way in many stations. Although great advances have been made in the area of simulation and fundamental
understanding of deep-fat frying, models that can predict changes in the product structure and volume as well as oil absorption during frying and after frying are still
required. A fundamental physics-based model of a continuous frying process is another area of critical need.

C2. Traditional Thermal Processing (Canning) Mathematical models through the use of computer simulation were developed at the Florida station for the
analysis, design, optimization and control of thermal processes used in canned food sterilization. These models can be used to predict the product temperature
history at any specified location within the can for any set of processing conditions and container size; thus, precluding the need to carry out repeated heat
penetration tests in the laboratory or pilot plant for alternate process designs. A second advantage is that the retort temperature need not be held constant, but can
vary in any prescribed manner.

An important application of these models is in the rapid evaluation of an unscheduled process deviation, such as when an unexpected drop in retort temperature
occurs during the process. The current practice in case of such a deviation is to set aside whole batch of product (for batch processing) to be judged safe by a
competent authority before releasing for shipment; otherwise the complete batch of product must be reprocessed or destroyed. Such practices are very costly and
inefficient and finding their alternatives is a critical need for the canning industry. The models resulting from this project are now being applied toward development of
intelligent on-line computer-based retort control systems capable of rapid evaluation, on-line correction, and printed documentation of any process deviations that
should occur while the process is still underway in real time. This would allow for the release of all product batches on schedule with full documentation in
compliance with government regulations (Teixeira et al., 1999). These models have already been adopted for routine use by the National Food Processors
Association (NFPA), and have been modified for application to intelligent on-line process control by firms specializing in instrumentation and control systems for the
food industry. The net impact of this work has been significant cost reduction while assuring food safety at maximum quality.

In another study, a fundamental and comprehensive model showed the development of broken heating during sterilization of canned starch dispersions (Yang and
Rao, 1998b). This quantitative understanding of heating of starch containing foods can have major impact in the improvement of thermal processes for such foods.

C3. Microwave Sterilization Use of microwaves instead of, or in combination with, conventional heating can produce sterilized foods of much improved quality.
Significant advances were made in developing accurate and comprehensive pictures of microwave food sterilization (Zhang and Datta, 1999). Extensive numerical
modeling and experimentation using chemical marker formation to verify models was performed. Unlike conventional sterilization, heating patterns can change
qualitatively with geometry and properties (composition) of the food material and an optimal heating is possible with their suitable combinations. Combined with
chemical marker yield measurements, the numerical model can give comprehensive descriptions of the spatial time- temperature history, and thus be used to verify
and establish microwave sterilization processes.

JOURNALS

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Bamnger, S.A., Bennett, M. A., and Bash, W. D. 1999. Effect of nitrogen fertilizer levels and fruit maturity on tomato peeling efficiency. Journal of Vegetable Crop
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Ho, K.G., Wilson, L.A. and Sebranek, J. 1997. Dried soy tofu powder effects on frankfurters and pork sausage patties. J. Food Science. 62:434-437.

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Ma, L., A. Grove and G. V. Barbosa-Canovas. 1996. "Viscoelastic Characterization of Surimi Gel: Effects of Setting and Starch." Journal of Food Science 61(5)
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Ma, L., M. A. Drake, G. V. Barbosa-Canovas and B. G. Swanson. 1997. "Rheology of Full-Fat and Low-Fat Cheddar Cheeses as Related to Type of Fat
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Ma, L., M. A. Drake, G. V. Barbosa-Canovas and B. G. Swanson. 1996. "Viscoelastic Properties of Reduced-Fat and Full-Fat Cheddar Cheeses." Journal of
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Maheshwari, P., Murphy, P. A. and Nikolov, Z. L. 1997. Characterization and application of porcine liver aldehyde oxidase in the off-flavor reduction of soy
proteins. J. Agric. Food Chem. 45: 2488-2494.

Malave, J., G. V. Barbosa-Canovas and M. Peleg. 1985. "Comparison of the Compaction Characteristics of Selected Food Powders by Vibration, Tapping and
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Malave, J., G. V. Barbosa-Canovas, M. Peleg and V. B. Zemelman. 1986. "Kinetic Models for the Attrition of Instant Coffee." In: Particulate and Multiphase
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Mallikarjunan, P., Chinnan, M.S., Balasubramaniam, V.M. and Phillips, R.D. 1997. Edible coatings for deep-fat frying of starchy products. Lebensm.-Wiss. U.
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Marangom, A.G. and Hartel, R.W. 1998. Visualization and Structural Analysis of Fat Crystal Networks, Food Technol., 52(9): 46-51.

Martin, 0., B-L. Qin, F-J. Chang, G. V. Barbosa-Canovas and B. G. Swanson. 1997. "Inactivation of Escherichia coli in Skim Milk by High Intensity Pulsed
Electric Fields." Journal of Food Processes Engineering 20:317-336.

Martin, 0., H. Vega-Mercado, B-L. Qin, F-J. Chang, G. V. Barbosa-Canovas and B. G. Swanson. 1997. "Inactivation of Escherichia coli Suspended in Liquid Egg
Using Pulsed Electric Fields." Journal of Food Processing and Preservation 21:193-208.

Martin, 0., Q. Zhang, A. J. Castro, G. V. Barbosa-Canovas and B. G. Swanson. 1994. "Pulse Electric Fields of High Voltage to Preserve Foods. Microbiological
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Martinez, R.M., P.L. Dawson, H.R. Ball, Jr., K.R. Swartzel, S.E. Winn and F.G. Giesbrecht. 1995. The effects of ultra pasteurization with and without
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Martinez-Padilla, L. P., A. C. Arzate-Lopez, V. A. Delgado-Reyes and G. V. Barbosa-Canovas. 1997. "Measurement and Prediction of the Pressure Drop Inside
a Pipe: The Case of a Model Food Suspension with a Newtonian Phase." Journal of Food Process Engineering 20(6):477-497.

Martinez-Padilla, L. P., L. Comejo-Romero, C. M. Cruz-Cruz, C. C. Jaquez-Huacuja arid G. V. Barbosa-Canovas. 1999. "Rheological Characterization of a
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Martinez-Padilla, L. P., M. M. Gongora-Nieto, J. L. Vergara-Acall, F. J. Lopez-Martinez and G. V. Barbosa-Canovas. "Flow Behavior Inside a Horizontal Pipe of
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Mashi, S.J., Flores, R.A., and Trivedi, R. 1996. Dynamics of solidification in 2% corn starch-water mixes: Effect of variations in freezing rate on product
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Maul, F., Sargent, S.A., Huber, D.J., Balaban, M.O., Luzuriaga, D.A., Baldwin, E.A. 1997. Non-destructive quality screening of tomato fruit using "electronic
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Maul, F., Sargent, S.A., Balaban, M.O., Baldwin, E.A., and Sims, C.A. 1998. Aroma volatile profiles from ripe tomatoes are influenced by physiological maturity at
harvest: an application for electronic nose technology. J. Am. Soc. Hort. Sci. 123(6): 1094-1101.

McCarthy, K.L. and McCarthy M.J. 1997. Food quality prediction from process tomography and flow modeling. In: Proceedings, 1 a International Symposium on
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McCarthy, M.J. and McCarthy, K.L. 1996. Applications of Magnetic Resonance Imaging to Food Research. Magnetic Resonance Imaging. 14:799-802. Metin, S.
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Metin, S. and Hartel, R.W. 1998. Thermal Analysis of Isothermal Crystallization Kinetics in Blends of Cocoa Butter with Milk Fat or Milk Fat Fractions, J. AOCS,
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Miles, J.J. and Swartzel, K.R. 1995. Evaluation of continuous thermal processing using thermocouple data and calibrating reactions. J. Food Process Eng.
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Miles, J.J. and Swartzel, K.R. 1995. Development of sucrose inversion kinetics under conditions of continuous flow. J. Food Quality 18:369-378.

Mills, R.H., Daubert, C.R., Stewman, D.Y. and C. Church. 199X. Control of viscosity in modified barium swallow examinations. Dysphagia. Accepted for
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Mitek, M., Chang, K.C. and Wiesenbom, D. 1997. Effect of extraction conditions on the yield and physicochemical characteristics of sunflower pectin. Polish J.
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Moizuddin, S., Buseman, G., Fenton, A.M. and Wilson, L. A. 1999. Tofil production from soybeans or full-fat soyflakes using direct and indirect heating processes.
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Monsalve-Gonzalez, A., G. V. Barbosa-Canovas, A. McEvily and R. lyengar. 1995. "Inhibition of Enzymatic Browning in Apple Products by 4-Hexylresorcinol."
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Monsalve-Gonzalez, A., G. V. Barbosa-Canovas and R. P. Cavalieri. 1993. "Mass Transfer and Textural Changes during Processing of Apples by Combined
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Monsalve-Gonzalez, A., G. V. Barbosa-Canovas, B. G. Swanson and R. P. Cavalieri. "Textural and Structural Changes in Apples Processed by Combined
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Monsalve-Gonzalez, A., G. V. Barbosa-Canovas, R. P. Cavalieri, A. McEvily and R. lyengar. 1993. "Control of Browning During Storage of Apple Slices
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Moreira, R.G. and Barrufet, M.A. 1995. Spatial distribution of oil after deep-fat frying from a stochastic model. J. of Food Engineering. 27(2): 205-220.

Moreira, R.G. and Barrufet, M.A. 1998. A new approach to describe oil absorption in fried foods: a simulation study. Journal of Food Engineering. 35:1-22.

Moreira, R.G. and Palau, J. 1995. Deep-fat frying of tortilla chips- an engineering approach J Food Tech. 49(4): 146-150.

Moreira, R.G., Lo, T. and Castell-Perez, M.E. 1995. Rheological changes in cooked corn meal dough to differences in moisture content. Food Science and
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Moreira, R.G., Palau, J.and Sun, X. 1995. Simultaneous heat and mass transfer during deep fat frying of tortilla chips. J. of Food Processing Engineering.
18:307-320.

Moreira, R.G., Palau, J. and Sweat, V. 1995. Thermal and physical properties of tortilla chips as a function of frying time. J. of Food Processing and Preservation.
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Moreira, R.G., Sun, X. and Chen, Y. 1997. Factors affecting oil uptake in tortilla chips in deep fat frying. J. of Food Engineering. 31(4): 485-498.

Mukherjee, D., Puri, V. M. and Anantheswaran, R. C. 1997. Measurement of coupled heat and moisture transfer coefficients for selected vegetables. Drying
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Murakami, E. G., Sweat, V. E., Sastry, S. K., Kolbe, E., Hayakawa, K., and Datta, A. K. 1995 Recommended design parameters for thermal conductivity probes
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Murakami, E.G., Sweat, V.E., Sastry, S.K. and Kolbe, E. 1996. Analysis of various design and operating parameters of thermal conductivity probe. J. Food Engr.
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Murano, P.S., Brennan, R.E., Shenoy, K. and Moreira, R.G. 1999. Application of high hydrostatic pressure to produce safe and long-lasting fresh pork sausage. J.
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Muriana, P. M., Hou, H. and Singh, R. K. 1996. A flow-injection system for studying heat motivation of Listeria monocytogenes and Salmonella enteritidis in liquid
whole egg. J. Food Protection 59(2):121-126. Murphy, P.A. 1996. History of technology development for vitamin A fortification of foods for developing countries.
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Murphy, P.A., Chen, H.P., Hauck, C.C. and Wilson, L.A. 1997. Soybean storage protein composition and torn quality. Food Technol. 51(3): 86-88,110.

Murphy, P.A., Song, T.T., Buseman, G. and Barua, K. 1997. Isoflavones in soy-based infant formula. J. Agric. Food Chem. 45:4635-4638.

Ndi, Embola E., A. K. Dunker, G. V. Barbosa-Canovas and L. 0. Luedecke. "A Calorimetric and Spectroscopic Study of? -Lactoglobulin-Sodium Polypectate
Interactions." Journal of Dairy Science. In Press.

Ndi, E. E., B. G. Swanson, G. V. Barbosa-Canovas and L. 0. Luedecke. 1996. "Rheology and Microstructure of? -Lactoglobulin-Sodium Polypectate Gels."
Journal of Food and Agriculture Chemistry 44:86-92.

Ndi, E. E., C. J. Brekke and G. V. Barbosa-Canovas. 1994. 'Thermal Gelation of Duck Breast and Leg Muscle Proteins." Journal of Muscle Foods 5:27-36.

Ni, H. and Datta, A.K. 1998. Moisture, oil, and energy transport during deep-frying of food materials. Accepted pending revisions in the Transactions of the
Institution of Chemical Engineers.

Ni, H. and Datta, A. K. 1999. Heat and moisture transfer in the baking of potato. Accepted pending revisions in the Journal of Drying Technology.

Ni, H., Datta, A. K. and Parmeswar, R. 1997. Moisture loss as related to heating uniformity in microwave processing of solid foods. Accepted pending revisions by
the Journal of Food Process Engineering

Ni, H., Datta, A. K. and Torrance, K. E. 1999. Moisture transport in intensive microwave heating of wet materials: A multiphase porous media model. International
Journal of Heat and Mass Transfer. 42(8): 1501-1512.

Njie, D. N., Rumsey, T. R. and Singh, R. P. 1998. Thermal properties of cassava, yam and plantain. Journal of Food Engineering 37:63-76.

Okechukwu, P. E. and Rao, M. A. 1995. Influence of granule size on viscosity of cornstarch suspension. J. Texture Studies. 26: 501-516.

Okechukwu, P. E. and Rao, M. A. 1996. Kinetics of cowpea starch gelatinization based on granule swelling. Starch/Starke. 48:43-47.

Okechukwu, P. E. and Rao, M. A. 1996. Role of granule size and size distribution in the viscosity of cowpea starch dispersions heated in excess water. J. Texture
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Okechukwu, P. E. and Rao, M. A. 1997. Calprimetric and rheological behavior of cowpea protein plus starch (cowpea and corn) gels. Food Hydrocolloids. 11:
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Ofoli, R.Y. and Prieve, D.C. 1997. Small angle Rayleigh light scattering by relatively large particles. Langmuir 13:4837-4842.

Onwulata, C.I., Mulvaney, S.J. and Hsieh, F. 1994. System analysis as the basis for control of density of extruded corn meal. Food Control, 5:39-48.

Orangi, S., Sastry, S.K. and Li, Q. 1998. A numerical investigation of electroconductive heating of solid-liquid mixtures. Int. J. Heat Mass Transfer 41(14):
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Ortega-Rivas, E., E. Zarate-Rodriguez and G. V. Barbosa-Canovas. 1998. "Apple Juice Pasteurization Using Ultrafiltration and Pulsed Electric Fields."
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Pagan-Toro, R., S. Esplugas, M. M. Gongora-Nieto, G. V. Barbosa-Canovas and B. G. Swanson. 1998. "Inactivation of Bacillus Subtilis Spores Using High
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Palazoglu, T. K., and Balaban, M.O. 1998. Supercritical CO 2 extraction of lipids from roasted pistachio nuts and evaluation of the remaining meal. Transactions of
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Palou, E., A. Lopez-Malo, G. V. Barbosa-Canovas, J. Welti-Chanes and B. G. Swanson. 1999. "Polyphenoloxidase Activity and Color of Blanched and High
Hydrostatic Pressure Treated Banana Puree." Journal of Food Science 64(1):42-45.

Palou, E., A. Lopez-Malo, G. V. Barbosa-Canovas, J. Welti-Chanes, P. M. Davidson and B. G. Swanson. 1998. "Effect of Oscillatory High Hydrostatic Pressure
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Palou, E., A. Lopez-Malo, G. V. Barbosa-Canovas, J. Welti-Chanes and B. G. Swanson. 1997. "Effect of Water Activity on High Hydrostatic Pressure Inhibition
of Zygosaccharomyces bailii." Letters of Applied Microbiology 24:417-420.

Palou, E., A. Lopez-Malo, G. V. Barbosa-Canovas, J. Welti-Chanes and B.G. Swanson. 1997. "High Hydrostatic Pressure as a Hurdle for Zygosaccharomyces
bailii Inactivation." Journal of Food Science 62(4):855-857.

Palou, E., A. Lopez-Malo, G. V. Barbosa-Canovas, J. Welti-Chanes and B. G. Swanson. 1997. "Kinetic Analysis of Zygosaccharomyces bailii Inactivation by
High Hydrostatic Pressure." Lebensmittel-Wissenschaft und-Technologie 30:703-708.

Palou, E., G. V. Barbosa-Canovas, B. G. Swanson, A. Lopez-Malo and J. Welti-Chanes. 1997. "High Hydrostatic Pressure Inactivation Kinetics of
Zygosaccharomyces bailii." In: Engineering & Food at ICEF 7. Part 1. R. Jowitt, Ed. Academic Press. D13-D16.

Palou, E., A. Lopez-Malo, G. V. Barbosa-Canovas, J. Welti-Chanes, P. M. Davidson and B. G. Swanson. 1998. "High Hydrostatic Pressure Come-Up Time and
Yeast Viability." Journal of Food Protection 61(12):1657-1660

Palou, E., A. Lopez-Malo, G. V. Barbosa-Canovas, J. Welti-Chanes and B. G. Swanson. 1998. "Oscillatory High Hydrostatic Pressure Inactivation of
Zygosaccharomyces bailii." Journal of Food Protection 61(9):1213-1215.

Panigrahi, S., Wiesenbom, D., Orr ,P., Schaper, L. and Bierwagen, G.. 1996. Spectral reflectance properties of French fries. Appl. Engr. Ag. 12(6): 721-724.

Parsons, M.H., Hsieh, F. and Huff, H.E. 1996. Extrusion cooking of corn meal with sodium bicarbonate and sodium aluminum phosphate. J. Food Proc. Preserv.
20:221-234.

Pascall, M.A., Zhang, Q.H., Burgess, G., Harte, B.R. and Wood, D.M. 1998. Integrity of preformed sealed plastic cups put to the test. J. Pkgng. Technol. & Eng.,
March 33-38.

Patience, D. and Hartel, R.W. 1999. Crystallization and Pressure Filtration of Anhydrous Milk Fat: Mixing Effects, J. AOCS, 76(5):, 585-594.

Peng, J., Huff, H.E. and Hsieh, F. 1994. An RTD determination method for extrusion cooking. J. Food Proc. Preserv. 18:263-277.

Pernell, C.W., Foegeding, E.A. and Daubert, C.R. 199X. Measurement of the yield stress of protein foams by vane rheometry. J. Texture Studies. Accepted for
publication.

Peters, S., Ulrich, J. and Hartel, R.W. 1999. Milk Fat Fractionation by Solid Layer Melt Crystallization, J. AOCS, 76(5): 579-584.

Peyre, F., Datta, A. K. and Seyler, C. E. 1997. Influence of the dielectric property on microwave oven heating patterns: application to food materials Journal of
Microwave Power and Electromagnetic Energy, 32(1): 3-15.

Pinthus, E. J., Singh, R. P., Rubnow, M. and Saguy, I. S. 1997. Effective water diffusivity in deep-fat fried restructured potato product. International Journal of
Food Science and Technology. 32:235-240.

Pinthus, E. J., Singh, R. P., Saguy, I. S. and Fan, J. 1998. Formation of resistant starch during deep-fat frying and its role in modifying mechanical properties of fried
patties containing corn, rice, wheat, or potato starch and water. Journal of Food Processing Preservation 22-283-301.

Pothakamury, U.R., A. Monsalve-Gonzalez, G. V. Barbosa-Canovas and B. G. Swanson. 1995. "High Voltage Pulsed Electric Field Inactivation of Bacillus Subtilis
and Lactobacillus Delbrueckii." Spanish Journal of Food Science and Technology 35 (1) :101-107.

Pothakamury, U. R., A. Monsalve-Gonzalez, G. V. Barbosa-Canovas and B.G. Swanson. 1995 "Inactivation of Escherichia coli and Staphylococcus aureus in
Model Foods by Pulsed Electric Field Technology." Food Research International 28(2): 167-171.

Pothakamury, U. R. and G. V. Barbosa-Canovas. 1995. "Controlled Release in Food Processing." Trends in Food Science and Technology 6(12) :397-406.

Pothakamury, U. R. and G. V. Barbosa-Canovas. 1993. "Membrane Technology In Food Processing." Fluid/Particle Separation Journal 6(3) :110-118.

Pothakamury, U. R., B. J. Barletta, G. V. Barbosa-Canovas and B. G. Swanson. 1993. "Inactivation of Microorganisms in Foods by Oscillating Magnetic Fields"
(in Spanish). Spanish Journal of Food Science and Technology 33(5) .-479-489.

Pothakamury, U. R., G. V. Barbosa-Canovas and B. G. Swanson. 1993. "Magnetic-Field Inactivation of Microorganisms and Generation of Biological Changes."
Food Technology 2:85-93.

Pothakamury, U. R., G. V. Barbosa-Canovas, B. G. Swanson and K. D. Spence. 1997. "Ultrastructural Changes in Staphylococcus aureus Treated with Pulsed
Electric Fields." Food Science and Technology International 3:113-121.

Pothakamury, U. R., G. V. Barbosa-Canovas and H. G. Schwartzberg. 1994. "Expressions in Food Processing." Fluid/Particle Separation Journal 7(4) : 172-183.

Pothakamury, U. R., G. V. Barbosa-Canovas, B. G. Swanson and R. Meyer. 1995. "Staying Fresh Under Pressure." Engineering World 8:29-34.

Pothakamury, U. R., G. V. Barbosa-Canovas, B. G. Swanson and R. S. Meyer. 1995. "The Pressure Builds for Better Food Processing." Chemical Engineering
Progress 91(3) :45-53.

Pothakamury, U. R., Vega-Mercado, Q. Zhang, G. V, Barbosa-Canovas and B. G. Swanson. 1996. "Effect of Growth Stage and Temperature on the Inactivation
of E. coli by Pulsed Electric Fields." Journal of Food Protection 59(11) :1167-1171.

Puri, V. M. and Anantheswaran, R.C. 1993. Finite element method in food processing – a review. J. Food Eng. 19:247-274.

Qin, B-L., F-J. Chang, G. V. Barbosa-Canovas and B.G. Swanson. 1995. "Nonthermal Inactivation of Saccharomyces cerevisiae in Apple Juice Using Pulsed
Electric Fields." Lebensmittel-Wissenschaft und-Technologie 28:564-568.

Qin, B-L., G. V. Barbosa-Canovas, B. G. Swanson, P. D. Pedrow and R. G. Olsen. 1998. "Inactivating Microorganisms Using a Pulsed Electric Field Continuous
Treatment System." IEEE Transactions on Industry Applications 34(1):43-50.

Qin, B-L., H. Vega-Mercado, U. R. Pothakamury, G. V. Barbosa-Canovas and B. G. Swanson. 1995. "Application of Pulsed Electric Fields for Inactivation of
Bacteria and Enzymes." Journal of The Franklin Institute 332(A) :209-220.

Qin, B-L., Q. Zhang, G. V. Barbosa-Canovas, B. G. Swanson and P. D. Pedrow. 1994. "Inactivation of Microorganisms by Pulsed Electric Fields with Different
Waveforms." IEEE Transactions on Dielectrics and Electrical Insulation 1(6) :1047-1057.

Qin, B-L., Q. Zhang, G. V. Barbosa-Canovas, B. G. Swanson and P. D. Pedrow. 1995. "Pulsed Electric Field Treatment Chamber Design Using a Finite Element
Method." Transactions of the ASAE 38(2) :557-565.

Qin, B-L., U. R. Pothakamury, G. V. Barbosa-Canovas and B. G. Swanson. 1996. "Nonthermal Pasteurization of Liquid Foods Using High Intensity Pulsed
Electric Fields." Critical Reviews in Food Science and Nutrition 36(6) :603-677.

Qin, B-L., U. R. Pothakamury, H. Vega- Mercado, 0. Martin, G. V. Barbosa-Canovas and B. G Swanson. 1995. "Food Pasteurization Using High Intensity Pulsed
Electric Fields." Food Technology 12:55-60.

Qiu, X. Sharma, S.K., Tuhela, L. Jia, M. and Zhang, Q.H. 1998. An integrated PEF pilot plant for continuous nonthermal pasteurization of fresh orange juice.
Trans. ASAE, 41(4): 1069-1074.

Qumtero-Ramos, A., A. L. Sanchez de La Paz, J. A. Meza-Velazquez, G. V. Barbosa-Canovas and A. Anzaldua-Morales. "Optimization of Stepwise Blanching of
Dehydrated Zucchini (Cucurbita pepo)" (in Spanish). Food Science and Technology International. In Press.

Ramkumar D. H. S., Bhattacharya, M., Menjivar, J. A. and Huang, T. A. 1996. Relaxation behavior and the application of integral constitutive equation for wheat
flour dough. J. Texture Studies. 27:517-544.

Ransom-Painter, K.L., Williams, S.D. and Hartel, R.W. 1997. Incorporation of Milk Fat and Milk Fat Fractions into Palm Kernel Oil Based Compound Coatings.
J. Dairy Sci. 80(10)' 22372248.

Rao, M. A. 1997. Pumping power requirements and role of viscosity during agitation of concentrated orange juice. Trans. 1997 Citrus Eng. Conference, ASME SE
Region XI. 43:45-63.

Rao, M. A. and Cooley, H. J. 1995. Rates of structure development during gelation and softening of high-methoxyl pectin-sodium alginate-fructose mixtures. Food
Hydrocolloids. 9: 229-235.

Rao, M. A., Cooley, H. J., and Liao, H-J. 1999. High temperature rheology of tomato puree and starch dispersion with a direct-drive viscometer. J. Food Process
Eng. 22:29-40.

Rao, M. A., Okechukwu, P. E., da Silva, P. M. S., and Oliveira, J. C. 1997. Rheological behavior of heated starch dispersions in excess water: role of starch
granule. Carbohydrate Polymers. 33: 273-283.

Rao, M.A. and StefFe, J.F. 1997. Measuring the yield stress of fluid foods. Food Technol. 51(2):50-52.

Rao, M. A. and Tattiyakul, J. 1999. Granule size and rheological behavior of heated tapioca starch dispersions. Carbohydrate Polymers. 38: 123-132.

Raso, J., G. V. Barbosa-Canovas and B.G. Swanson. 1998. "Sporulation Temperature Affects Initiation of Germination and Inactivation by High Hydrostatic
Pressure of Bacillus cereus." Journal of Applied Microbiology 85:17-24.

Raso, J., M. L. Calderon, M. M. Gongora-Nieto, G. V. Barbosa-Canovas and B. G. Swanson. 1998. "Inactivation of Mold Ascospores and Conidiospores
Suspended in Fruit Juices by Pulsed Electric Fields." Lebensmittel-Wissenschaft und-Technologie 31(7/8) :668-672.

Raso, J., M. L. Calderon, M. M. Gongora-Nieto, G. V. Barbosa-Canovas and B. G. Swanson. 1998. "Inactivation of Zygosaccharomyces bailii in Fruit Juices by
Heat, High Hydrostatic Pressure and Pulsed Electric Fields." Journal of Food Science 63(1): 1042-1044.

Raso, J., M. M. Gongora, G. V. Barbosa-Canovas and B.G. Swanson. 1998. "Influence of Several Environmental Factors on the Initiation of Germination and
Inactivation of Bacillus cereus by High Hydrostatic Pressure." International Journal of Food Microbiology 44:125-132.

Reddy, N.R., Solomon, H.M., Fingerhut, G.A., Rhodehamel, E.J., Balasubramaniam, V.M., and Palaniappan, S. 1999. Inactivation of Clostridium botulinum type E
spores by high pressure processing. J Food Safety (In Press)

Reina, L.D., Jin, Z.T., Zhang, Q.H. and Yousef, A.E. 1998. Inactivation of Listeria monocytogenes in milk by pulsed electric fields. J. Food Prot., 61(9):
1203-1206.

Requena, D.D., Hale, S.A., Green, D.P., McClure, W.F. and Farkas, B.E. 1999. Detection of discoloration in thermally processed blue crabmeat. J. Sci Food
Agric 79:786-791.

Robbers, M., Singh, R. P. and Cunha, L. M. 1997. Osmotic-convective dehydro freezing process for drying kiwifruit. Journal of Food Science. 62(5): 1039-1042,
1047.

Roberts, J. S., Balaban, M. 0., Zimmerman, R. and Luzuriaga, D. 1998. Design and testing of a prototype ohmic thawing unit. Computers and Electronics in
Agriculture. 19:211-222.

Rodenbush, C.M, Hsieh, F. and Viswanath, D.S. 1999. Density and viscosity of vegetable oils. J. Am. Oil Chem. Soc., in press.

Rodenbush, C.M., Viswanath, D.S. and Hsieh, F. 1999. A group contribution method for the prediction of thermal conductivity of liquids and its application to the
Prandtl number for vegetable oils. Ind. Eng. Chem. Res., in press.

Roy, S., Anantheswaran, R. C. and Beelman, R. B. 1995. Fresh mushroom quality as affected by modified atmosphere packaging. J. Food Sci. 60:334-340.

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Yeh, R. S., Anantheswaran, R. C., Shenk, J. and Puri, V. M. 1994. Determination of moisture profile in foods during microwave heating using vis-NIR
spectroscopy. Lebensmittel-Wissenschaft und Technologie 27(4) :358-362.

Yongsawatdigul, J., J.W. Park, E. Kolbe. Kinetics of texture degradation in Pacific whiting surimi. 1997a J. Food Process Engineering 20:433-452.

Yongsawatdigul, J., J.W. Park, E. Kolbe. 1997b. Degradation kinetics of myosin heavy chain of Pacific whiting surimi. J. Food Science. 62: 724-728.

Yongsawatdigul, J., J.W. Park, E. Kolbe. 1995. Electrical conductivity of Pacific whiting surimi paste during ohmic heating. J. Food Sci. 60(5):922-925,935.

Yongsawatdigul, J., J.W. Park, E. Kolbe, Y. Abudagga, M.T. Momssey. 1995 Ohmic heating maximizes gel functionality of Pacific Whiting surimi. J. Food Science.
60(1): 10-14

Yoo, B. and Rao, M. A. 1995. Yield stress and relative viscosity of tomato concentrates: effect of total solids and finisher screen size. J. Food Sci. 60: 777-779,
785.

Yoo, B. and Rao, M. A. 1996. Creep and dynamic rheological behavior of tomato concentrates: effect of concentration and finisher screen size. J. Texture Studies
27: 451-459.

Yoo, B., Rao, M. A., and Steffe, J. F. 1995. Yield stress of food suspensions with the vane method at controlled shear rate and shear stress. J. Texture Studies 26:
1-10.

Zhang, Q., G. V. Barbosa-Canovas and B. G. Swanson. 1995. "Engineering Aspects of Pulsed Electric Field Pasteurization." Journal of Food Engineering 25(2)
:261-281.

Zhang, D. and Bhattacharya, M. 1996. Numerical simulation of entry flows of corn meal J Food Eng. 28:323-339.

Zhang, Q., F-J. Chang, G. V. Barbosa-Canovas and B. G. Swanson. 1994. "Inactivation of Microorganisms in Semisolid Model Foods Using High Voltage Pulsed
Electric Fields." Lebensmittel-Wissenschaft und-Technologie 27:538-543.

Zhang, S., Datta, A. K. and Ni, H. 1995. The stochastic finite element method for analyzing conduction heat transfer in foods. Transactions of the Chinese Society
of Agricultural Engineering. 11(2): 143-148.

Zhang, Z. and Hartel, R.W. 1996. A multilayer freezer for freeze concentration of liquid milk. J. Food Eng. 29(1): 23-38.

Zhang, Q., A. Monsalve-Gonzalez, G. V. Barbosa-Canovas and B. G. Swanson. 1994. "Inactivation of Escherichia coli and Saccharomyces Cerevisiae by Pulsed
Electric Fields under Controlled Temperature Conditions." Transactions of the ASAE 32(2) :581-587 (1995 ASAE Paper Award).

Zhang, Q., A. Monsalve-Gonzalez, B-L. Qin, G. V. Barbosa-Canovas and B. G. Swanson. 1994. "Inactivation of Saccharomyces cerevisiae by Square-Wave and
Exponential-Decay Pulsed Electric Fields." Journal of Food Process Engineering 17(4) :469-478.

Zhang, Q., B-L. Qin, G. V. Barbosa-Canovas and B. G. Swanson. 1995. "Inactivation of Escherichia coli for Food Pasteurization by High-Intensity-Short-Duration
Pulsed Electric Fields." Journal of Food Processing and Preservation 19:103-118.

Zhao, Y., B. Flugstad, E. Kolbe, J.W. Park, J.H. Wells. Using capacitive (radio frequency) dielectric heating in food processing and preservation - a review. J.
Food Process Engineering (In Press).

Zhao, Y., E. Kolbe, C. Craven. 1998. Simulation of onboard chilling and freezing of albacore tuna. J. of Food Science. 63(5):751-755

Zhao, Y., E. Kolbe, B. Flugstad. 1999. A method to characterize electrode corrosion during ohmic heating. J. Food Process Engineering 22(1999):81-89

Zhou, L., Puri, V. M. and Anantheswaran, R. C. 1994. Measurement of coefficients for simultaneous heat and mass transfer in food products. Drying Technology
12(3): 607-627.

Zhou, L., Puri, V. M., and Anantheswaran, R. C. 1994. Effect of temperature gradient on moisture migration during microwave heating. Drying Technology. 12(4):
777-798.

Zhou, L. M., Puri, V. M., Anantheswaran, R. C. and Yeh, G. 1995. Finite element modeling of heat and mass transfer in food materials during microwave heating -
model development and validation. J. Food Eng. 25:509-529

BOOKS

Balaban, M.O. 1999. Textbook on Food Engineering with 12 chapters and its associated software package. The final manuscript is in review by the publisher (CRC
Press, Boca Raton, FL).

Barbosa-Canovas, G. V., A. Ibarz-Ribas, S. Garza, V. Gimeno, L. ma and B.J. Barletta. 1999. Food Technology Laboratory Manual (in Spanish). Zaragoza,
Spain : Acribia, S.A.

Barbosa-Canovas, G. V., S. Lombardo, G. Narsimhan and M. R. Okos, Eds. 1997. New Frontiers in Food Engineering. Proceedings of the fifth CoFE. New
York: AlChE.

Barbosa-Canovas, G. V., L. Ma and B.J. Barletta. 1997. Food Engineering Laboratory Manual. Lancaster, PA: Technomic Publishing Co., Inc.

Barbosa-Canovas, G. V., U.R. Pothakamury, M. Gongora Nieto and B. G. Swanson. 1999. " Preservation of foods with Pulsed Electric Fields. San Diego:
Academic Press.

Barbosa-Canovas, G. V., U. R. Pothakamury, E. Palou and B. G. Swanson. 1997 Nonthermal Preservation of Foods. New York: Marcel Dekker.

Barbosa-Canovas, G. V. and H. Vega-Mercado. 1996. Dehydration of Foods. New York: Chapman & Hall.

Barbosa-Canovas, G. V. and J. Welti-Chanes, Eds. 1995. Food Preservation by Moisture Control: Fundamentals and Applications. ISOPOW Practicum II.
Lancaster, PA: Technomic Publishing Co., Inc.

Datta, A. K. 1999. Biological and Bioenvironmental Transport Processes. Marcel Dekker, Inc., New York, NY. Completed and self-published 400 page
textbook that will be republished by Marcel Dekker in May 2000.

Datta, A. K. and Anantheswaran, R. C. (Ed.) 2000. Handbook of Microwave Technology for Food Applications. Marcel Dekker, Inc., New York, NY.
Expected publication date April 2000.

Fito, P., E. Ortega-Rodriguez and G. V. Barbosa-Canovas, Eds. 1997. Food engineering 2000. New York: Chapman & Hall.

Hartel, R.W., Howell, T.A. and Hyslop, D.B. 1997. Math Concepts for Food Engineering. Technomics, Lancaster, PA.

Hasenhuetti, G.L and Hartel, R.W. (Ed.). 1997. Food Emulsijiers and Their Applications. Chapman and Hall, NY.

Heldman, D.R. and Hartel, R.W. 1997. Food Processing. Chapman and Hall, NY. Ibarz-Ribas, A. and G. V. Barbosa-Canovas. 1999. Unit Operations in Food
Engineering (in Spanish).

Lancaster, PA: Technomic Publishing Co., Inc. Ma, L., L. Obalda, D.C. David and G. V. Barbosa-canovas. 1999. Engineering Properties of Food and Other
Biological Products.

St. Joseph, MI: ASAE. Moreira, R.G., Castell-Perez, M.E. and Barrufet, M.A. 1999. Deep-Fat Frying: Fundamental and Applications. Aspen Publisher.
Boston, MA.

Rao, M. A. 1999. Rheology of Fluid and semisolid Foods: Principles and Applications, Aspen Publishers, Inc., Gaithersburg, MD.

Rao, M. A. and Hartel, R. W. (Ed.) 1998. Phase/State Transitions in Foods: Chemical, Structural, and Rheological Changes, Marcel Dekker, Inc., New
York.

Rao, M. A. and Rizvi, S. S. H. (Ed.) 1995. Engineering Properties of Foods, 2nd ed. Marcel Dekker, Inc., New York.

Rotstein, E., Singh, R. P. and Valentas, K. 1997. Handbook of Food Engineering Practice. CRC Press, Inc., Baco Raton, Florida.

Singh, R. K. (Ed.), 1995. Food Process Design and Evaluation, Technomic Publishing Co., Lancaster, PA, 257 pp.

Singh, R. P. 1996. Computer Applications in Food Technology. Academic Press, San Diego, California.

Singh, R. P. and Heldman, D. R. 1997. Introduccion a la Ingenieria de los Alimentos, S. A. Acribia (Ed.), Academic Press, Inc., Orlando, Florida.

Singh, R.K. and Rizvi, S. S. H. (Ed.), 1995. Bioseparation Processes in Foods, Marcel Dekker, New York. 469pp.

Steffe, J.F. 1996. Rheological Methods in Food Process Engineering, 2nd ed. Freeman Press, East Lansing, Michigan.

Taub, I. A., and Singh, R. P. 1998. Food Storage Stability. CRC Press, Inc., Bacon Raton, Florida.

BOOK CHAPTERS

Balaban, M.O. and Luzuriaga, D.A. 1997. Automated sensory procedures for shrimp. Fish Inspection, Quality Control andHACCP: A Global Focus, R.E.
Martin, R.L. Collette and J.W. Slavin (Ed.), p. 509-520. Technomic Publishing Co. Lancaster, PA.

Balaban, M.O., Luzuriaga, D., Yerlan, S. and Hasan, R. 1997. Automated quality evaluation of shrimp. Engineering and Food in ICEF 7, R. Jowitt (Ed.), p.
A105-108. Sheffield Academic Press.

Balaban, M.O., O'Keefe, S. and Polak, J.T. 1996. Supercritical fluid extraction of algae. Supercritical Fluid Extraction in Oil and Lipid Chemistry, J. King and
G. List (Ed.), p 247-266. AOCS Monograph.

Balaban, M.O., Roberts, J., Luzuriaga, D., and Hasan, R. 1997. Engineering and Food in ICEF 7, R Jowitt, (Ed.) p. C53-56. Sheffield Academic Press.

Balaban, M.O. and Ural, S. 1997. Personal computers in food engineering education. Engineering and Food in ICEF 7, R. Jowitt (Ed.), p. Q9-12. Sheffield
Academic Press.

Balaban, M.O., Vega, P., Sims, C., O'Keefe, S. and Comell, J. 1997. Supercritical CO 2 extraction of carotenes from carrots. Engineering and Food in ICEF 7,
R. Jowitt (Ed.) p. 125-128. Sheffield Academic Press.

Balasubramaniam, V. M. and Chinnan , M. S. 1997. Role of packaging in quality preservation of frozen foods. Quality in Frozen Food, M. C. Erickson, and Y.
-C. Hung. (Ed.), p. 296-306. Chapman & Hall.

Barbosa-Canovas, G. V., U. R. Pothakamury and B. G. Swanson. 1995. "State-of-the Art Technologies for the Stabilization of Foods by Nonthermal Processes:
Physical Methods." In: Food Preservation by Moisture Control: Fundamentals and Applications. G. V. Barbosa-Canovas and J. Welti-Chanes, Eds. pp.
493-532.

Barbosa-Canovas, G. V., B-L. Qin and B. G. Swanson. 1997. "The Study of Critical Variables in the Treatment of Foods by Pulsed Electric Fields." In: Food
Engineering 2000. P. Fito, E. Ortega-Rodriguez and G. V. Barbosa-Canovas, Eds. pp. 141-159.

Barbosa-Canovas, G. V., B. L. Qin, B. G. Swanson. 1998. "Biological Effects Induced by Pulsed Electric Fields of High Intensity." In: Tecnologias Avanzadas en
Esterilizacion y Seguridad de Alimentosy Otros Productos. M. Rodrigo, A. Martinez, S. M. Fiszman, C. Rodrigo, and A. Mateau, Eds. pp. 151 -165.

Barbosa-Canovas, G. V., B. L. Qin, B. G. Swanson. 1998. Preservation of Foods by Pulsed Electric Fields: System Design and Key Components." In:
Tecnologias Avanzadas en Esterilizacion y Seguridad de Alimentos y Otros Productos. M. Rodrigo, A. Martinez, S. M. Fiszman, C. Rodrigo, and A. Mateau,
Eds. pp. 151-165.

Barbosa-Canovas, G. V., M. F. San Martin, F. M. Harte and B. G. Swanson. "Magnetic Fields as a Potential Nonthermal Technology for the Inactivation of
Microorganisms." In: Inactivation of Foodbome Microorganisms. V. K. Juneja and J. N. Sofos, Eds. (in press).

Barbosa-Canovas, G. V., H. Vega-Mercado and E. Ortega-Rivas. 1997. "Propiedades Fisicas m. Caracterizacion de Alimentos en Polvo." In: Temas en
Tecnologia de Alimentos. Vol. I. J. M. Aguilera, Ed. pp. 289-337.

Cristianini, M. and Singh, R. P. 1997. Determination of thermal properties offish and seafood using transient methods. Engineering & Food at ICEF 7, Part I, R.
Jowitt (Ed.), p. Al -A4. Sheffield Academic Press.

Datta, A. K. 1999. Fundamentals of heat and moisture transport for microwave processing of foods. To be published in Handbook of Microwave Technology for
Food Applications. A. K. Datta and R. C. Anantheswaran, (Ed.), Marcel Dekker, Inc., New York.

Daubert, C.R. and Foegeding, E.A. 1998. Principles of food rheology. Introduction to the Chemical Analysis of Foods, S. Suzanne Nielsen (Ed.), Jones and
Bartlett Publisher, Inc., Boston.

Daubert, C.R. and Steffe, J.F. 1999. Dimensional Analysis of the Electrhorheological Behavior of Milk Chocolate. New Techniques in the Analysis of Foods,
M.H. Tunick, S.A. Palumbo, and P.M. Fratamico (Ed.), Plenum Publishing Corporation, New York.

Fabian, J., Hartel, R.W. and Ulrich, J. 1996. Growth and dissolution rate dispersion in sucrose crystals. Crystal Growth of Organic Materials, A.S. Myerson,
D.A. Green, and P. Meenan (Ed.), p. 216-219. ACS Conference Proceeding Series.

Farkas, B.E. and Farkas, D.F. 1997. Material and Energy Balances. Ch. 7 in The Food Engineering Handbook, R.P. Singh, E. Rotstein and K.J. Valentas (Ed.)
CRC Press, Inc., Boca Raton, FL.

Femandez-Molina, J. J., G. V. Barbosa-Canovas and B. G. Swanson. "Inactivation of Microorganisms by High Intensity Pulsed Electric Fields." In: Inactivation
ofFoodbome Microorganisms. V. K. Juneja and J. N. Sofos, Eds. (in press, expected publication date: July 2000)

Gomes Da Silva, M., Stroeve, P. and Singh, R. P. 1997. Analysis of oil penetration in foods during drying using a single pore approach. Engineering & Food at
ICEF 7, Part 2, R. Jowitt (Ed.), p. G57-G60. Sheffield Academic Press.

Hartel, R.W. 1996. Controlling crystallization in foods. Ch. in Crystal Growth of Organic Materials, A.S. Myerson, D.A. Green and P. Meenan (Ed.), p.
172-177. ACS Conference Proceeding Series.

Hartel, R.W. 1998. Mechanisms and kinetics ofrecrystallization in ice cream. The Properties of Water in Foods: ISOPOW 6, DS Reid (Ed.), p. 287-319. Blackie,
London.

Hartel, R.W. 1998. Phase transitions in chocolates and coatings. Phase/State Transitions in Foods, M.A. Rao and R.W. Hartel (Ed.), p. 217-252. Marcel
Dekker, New York

Hartel, R.W. 1998. Phase transitions in ice cream. Phase/State Transitions in Foods, M.A. Rao and R.W. Hartel (Ed.), p. 327-368. Marcel Dekker, New York.

Hsieh, F. 1999. Extrusion and extrusion cooking. Wiley Encyclopedia of Food Science and Technology, pp. 699-706, Frederick J. Francis (Ed.), John Wiley &
Sons, New York, NY.

Hsieh, F. 1999. Ultrafiltration and reverse osmosis. Wiley Encyclopedia of Food Science and Technology, pp. 2614-2619, Frederick J. Francis (Ed.), John
Wiley & Sons, New York, NY.

Hubbard, L.J. and Farkas, B.E. 1998. Determination of the convective heat transfer coefficient during immersion fiying. Drying '98 Vol. A, C.B. Akritidis, D.
Marinos-Kouris and G.D. Saravakos (Ed.), p. 781-788. Ziti Publishing Co., Thessaloniki, Greece.

Jin, Z., Hsieh, F. and Huff, H.E. 1997. Effects of ingredients and screw speed on physical properties of corn meal in twin screw extrusion. Proceedings of the 4th
Conference of Food Engineering, pp.44-46. G. Narsimhan, M.R. Okos and S. Lombardo (Ed), Purdue University, West Lafayette, IN.

Kader, A. A., Singh, R. P. and Mannapperuma, J. D. 1998. Technologies to extend the refrigerated shelf life of fresh fruits. Food Storage Stability, I. A. Taub,
and R. P. Singh (Ed.), p. 419-434. CRC Press.

Kauten, R. and McCarthy, M.J. 1995. Applications ofNMR Imaging in Processing of Foods. Food Processing Recent Developments. GaonkarA.N. (Ed.), p.
1-22. ElsevierNew York.

Kim, S-M., McCarthy, M.J., Bibbs, D. and Chen, P. 1998. Water in Tissue Structures by NMR and MRI. The Properties of Water In Foods ISOPOW 6. D.S.
Reid. (Ed.), p. 30-40. Blackie Academic & Professional New York.

Kolbe, E. Freezing technology. IN Surimi and Surimi Seafoods. J.W. Park, Ed. Marcel Dekker; In press.

Li, Y., Lu, Q., Huff, H.E. and Hsieh, F. 1997. Using a co-rotating self-wiping twin-screw extruder as an on-line rheometer. Proceedings of the 4th Conference of
Food Engineering. pp.97-100. G. Narsimhan, M.R. Okos and S. Lombardo (Ed), Purdue University, West Lafayette, IN.

Lin, Y., Huff, H.E., Hsieh, F. and lannotti, E. 1997. Flexible polyurethane foam extended with corn starch. Cereals: Novel Uses and Processes, pp.27-33, G.M.
Campbell, C. Webb and S.L. McKee (Ed.), Plenum Press, New York, NY.

Lopes da Silva, J. A. L. and Rao, M. A. 1998. Rheology of food polymer structures during gelation and melting. Formulation Science - Volume 1, C. L. Foy, D.
W. Pritchard and G. B. Beestman (Ed.), p. 424-442. CRC Press, Boca Raton, FL.

Lopes da Silva, J. A., Rao, M. A., and Fu, J-T. 1998. Rheology of structure development and loss during gelation and melting. Phase/State Transitions in Foods:
Chemical, Rheological and Structural Changes, M. A. Rao and R. W. Hartel (Ed.), p. 111-156. Marcel Dekker, Inc. New York.

Lopez-Malo, A., M. S. Tapia, S. M. Alzamora, J. Welti-Chanes, M. M. Marcela Gongora-Nieto and G. V. Barbosa-Canovas. "Water Activity: Microbiology." In:
Wiley Encyclopedia of Food Science and Technology, 1 nd Edition. (in press).

Ma, L., F-J. Chang, M. Marcela Gongora-Nieto, G. V. Barbosa-Canovas and B. G. Swanson. "Food Pasteurization Using High-Intensity Pulsed Electric Fields:
Promising New Technology for Non-Thermal Pasteurization for Eggs." In: Proceedings of the Second International Symposium on Egg Nutrition and Newly
Emerging Ovo-Technologies. J. S. Sim, Ed. (in press).

Murphy, PA., Barua, K., Song, T.T. 1998. Soy Isoflavones in Foods: Database Development in American Chemical Society Symposium Series: Functional
Foods: Overview and Disease Prevention, Ed. T. Shibamoto. In press.

Nelson, S. 0. and Datta, A. K. 1999. Dielectric properties of food materials and electric field interactions. To be published in Handbook of Microwave
Technology for Food Applications. A. K. Datta and R. C. Anantheswaran (Ed.), Marcel Dekker, Inc., New York, NY

Okechukwu, P. E. and Rao, M. A. 1996. Kinetics ofcomstarch granule swelling in excess water. Gums & Stabilizers for The Food Industry 8, G. 0. Phillips, P.
A. Williams and D. J.Wedlock (Ed.), p. 49-57. The Oxford University Press, Oxford, U.K.

Okechukwu, P. E. and Rao, M. A. 1998. Rheology of structured polysaccharide food systems: starch and pectin, Polysaccharide Association Structures in
Food, R. H. Walter (Ed.), p. 289-328. Marcel Dekker, Inc., New York.

Palou, E., A. Lopez-Malo, G. V. Barbosa-Canovas and B. G. Swanson. "High Pressure Treatment in Food Preservation." 1999. In: Handbook of Food
Preservation. M. S. Rahman, Ed. pp.533-576.

Palou, E., A. Lopez-Malo, J. Welti-Chanes, G. V. Barbosa-Canovas and B. G. Swanson. 1999. "Importance of Water in Foods Preserved by High Hydrostatic
Pressure." In: Water Management in the Design and Distribution of Quality Foods. Y. H. Roos, R. B. Leslie and P. J. Lillford, Eds. pp. 481-501.

Park, J. W., J. Yongsawatdigul, E. Kolbe. 1998. Proteolysis and gelation offish proteins under ohmic heating (Book Chapter) In Process-Induced Chemical
Changes in Foods. F.Shahidi, C-T.Ho, N. Van Chuyen, ed. Plenum Press. New York

Ramaswamy, H. S. and Singh, R. P. 1997. Sterilization process engineering. Handbook of Food Engineering Practice, K. J. Valentas, E. Rotstein, and R. P.
Singh (Ed.), p. 37-69. CRC Press, Inc., Baco Raton, Florida.

Rao, M. A. 1995. Rheological properties of fluid foods. Engineering Properties of Foods, 2nd edition, M. A. Rao and S. S. H. Rizvi (Ed.), p. 1-53. Marcel
Dekker, Inc., New York.

Rao.M.A 1997. Engineering properties of foods: Current status. Food Engineering 2000, P. Fito, E. Oretga Rogriguez and G. Barbosa-Canovas (Ed.), p. 39-54.
International Thomson Publishing Co., New York.

Rao.M.A. 1997. Rheological properties of fluid foods: Recent developments. Food Engineering 2000, P. Fito, E. Oretga Rogriguez and G. Barbosa-Canovas
(Ed.), p. 55-63. International Thomson Publishing, New York.

Rao, M. A. and Vitali, A. A. 1999. Fruit juice concentration and preservation. Handbook of Food Preservation, S. Rahman (Ed.), p. 217-258, Marcel Dekker,
Inc., New York.

Resurreccion, A. V. A., Chinnan, M. S., Erickson, M. C., Hashim, I. H., Balasubramaniam, V. M., Mallikaqunan, P. and Liao, J .-H.. 1997. Consumer-based
approach in developing alternate packaging systems for fluid milk for the elderly. 1996 Packaging Yearbook. B. Blakistone (ed). National Food Processors
Association.

Saltiel, C. and Datta, A. K. 1998. Heat and mass transfer in microwave processing. Advances in Heat Transfer, 32:1-100.

Singh, R. P. 1995. Principles of heat transfer. Chapter 11 in Frozen and Refrigerated Doughs and Batters, K. Kulp, K. Lorenz, and J. Brummer (Ed.), American
Association of Cereal Chemists, Inc.

Singh, R. P. (Ed.). 1996. Food Engineering. The Engineering Handbook, p. 1779-1791. CRC Press, Inc., Baco Raton, Florida.

Singh, R. P. 1996. Food processing. In The New Encyclopaedia Britannica 19: 339-346,405.

Singh, R. P. 1996. Frozen prepared foods. In The New Encyclopaedia Britannica 19-400-402, 406.

Singh, R. P. 1997. Food engineering curricula North-American and Asian perspectives. Chapter 20 in Food Engineering 2000, P. Fito, E. Ortega-Rodriguez, and
G. V. Barbos-Canovas (Ed.), Chapman & Hall.

Singh, R. P. 1997. Time-temperature indicators. The Wiley Encyclopedia ofPackaging Technology, 2nd Edition, A. L. Brody, and K. S. Marsh (Ed.), p.
926-927. John Wiley & Sons, Inc.

Singh, R. P. 1998. Phase transition and transport phenomena in frying of foods. Phase/State Transitions in Foods, Chemical, Structural, and Rheological
Changes, M. A. Rao, and R W Hartel (Ed.), p. 369-390. Marcel Dekker, Inc.

Steffe, J. F. and Singh, R. P. 1997. Pipeline design calculations for Newtonian and non-Newtonian fluids. Handbook of Food Engineering Practice, K. J.
Valentas, E. Rotstein, and R. P. Singh (Ed.), p. 1-35. CRC Press, Inc., Baton Raton, Florida.

Stiefermann, K.M., Huff, H.E. and Hsieh, F. 1997. Twin-screw extrusion of corn meal with amaranth. Proceedings of the 4th Conference of Food Engineering,
pp. 141-145. G. Narsimhan, M.R. Okos and S. Lombardo (Ed.), Purdue University, West Lafayette, IN.

Tang, C., Hsieh, F. and Huff, H.E. 1997. The effect of wheat protein fractions and an emulsifier on spaghetti processing and qualities. Engineering & Food at
ICEF 7, pp.A81-A84, R. Jowitt (Ed.), Sheffield Academic Press, Sheffield, UK.

Teixeira, A.A. and Tucker, G.S. 1997. Critical Control Points for On-Line Computer Simulation and Control of Canned Food Sterilization. Food Engineering
2000. P. Fito, E. Ortega-Rodriguez, and G.V. Barbosa-Canovas, (Ed.), p. 291-307. Chapman & Hall,'International Thomson Publishing, New York.

Teixeira, A.A., Balaban, M.O. and Welt, B.A. 1997. Estimation of thermal death rate constants from innoculated cans of pea puree undergoing thermal processes.
Engineering and Food in ICEF-7, R. Jowitt, (Ed.), p. K41-44. Sheffield Academic Press.

Tiedtke, M., Ulrich, J. and Hartel, R.W. 1996. Solid layer melt crystallization - a fractionation process for milk Fat, Crystal Growth of Organic Materials, A.S.
Myerson, D.A. Green and P. Meenan, (Ed.), p. 137-144. ACS Conference Proceeding Series.

Vega-Mercado, H., M. Marcela Gongora-Nieto, G. V. Barbosa-Canovas and B. G. Swanson. 1999. "Nonthermal Preservation of Liquid Foods Using Pulsed
Electric Fields." In: Handbook of Food Preservation. M. S. Rahman, Ed. pp. 487-520.

Vijayan, J., Pan, Z. and Singh, R. P. 1997. Modeling heat transfer and destruction of E. Coli 0157:H7 during cooking of hamburger patties. Engineering & Food
at ICEF 7. Part 2, R. Jowitt (Ed.), p. K45-K48. Sheffield Academic Press.

Vijayan, J., and R. P. Singh. 1997. Sensitivity to processing conditions during frying of frozen foods. Engineering & Food at ICEF 7, Part 2, R. Jowitt (Ed.), p.
H49-H52. Sheffield Academic Press.

Wells, J. H. and Singh, R. P. 1997. Temperature tolerance of foods during distribution. Handbook of Food Engineering Practice, K- J. Valentas, E. Rotstein, and
R. P. Singh (Ed.), p. 405-423. CRC Press, Inc., Bacon Raton, Florida.

Wells, J. H. and Singh, R. P. 1998. Quality management during storage and distribution. Food Storage Stability, I. A. Taub, and R. P. Singh (Ed.), p. 369-386.
CRC Press.

Weiti, J., S. M. Alzamora, A. Lopez-Malo, M. S. Tapia, G. V. Barbosa-Canovas and E. Parada-Arias. 1999. "Role of Water in the Stability of Minimally or
Partially Processed Foods." In: Water Management in the Design and Distribution of Quality Foods. Y. H. Roos, R. B. Leslie and P. J. Lillford, Eds. pp.
503-532.

Wilson, L.A. 1995. Soy foods. Practical Handbook of Soybean Processing and Utilization, D.R. Erickson (Ed.), p. 428-459. AOCS Press and USB Press, St.
Louis. MO.

Wilson, L.A. 1996. Comparison of lipoxygenase-null and Lipoxygenase-containing soybeans for foods. Lipoxygenase and Lipoxygenase Pathway Enzymes, M.
Piazza (Ed.), p 209-225 AOCS Press, St. Louis, MO.

Yang, W. H., Datta, A. K., and Rao, M. A. 1997. Rheological and Calorimetric Behavior of Starch Gelatinization in Simulation of Heat Transfer. Engineering and
Food at ICEF 7 / Part 2, R. Jowitt (Ed.), p. K1-K5. Sheffield Academic Press, London.

Thome, A.E., Farkas, B.E. and Rutledge, G.R. 1997. Effect of food based contaminants on the integrity ofthermoformed seals. Paper 377 P, Engineering and
Food at ICEF 7, R. Jowitt (Ed.), Sheffield Academic Press, Sheffield, UK.

THESES AND DISSERTATIONS

Adieman, R. 1998. Lipid Emulsifier Interactions in Ice Cream. MS Thesis, Univ. of Wisconsin, Madison.

Ahn, H. 1995. Effects of Extrusion Temperature and Isolated Protein on the Physical and Chemical Properties of Fat-Reduced Pork Sausage Products. MS Thesis,
Univ. of Missouri, Columbia.

Ahza, A.B. 1995. Kinetics of Milk Fat Crystallization in a Continuous Crystallizer. Ph.D. dissertation, Univ. of Wisconsin, Madison. Arola, D.F. 1997.
Development of a Nuclear Magnetic Resonance Imaging-Based Viscometer. Ph.D. dissertation, Univ. of California, Davis. 315 p.

Azam, A.T.M. Safiul, 1997. Prediction ofBostwick Consistency for Tomato Products Using Pressure Drop Along a Pipe. MS Thesis, Ohio State Univ.

Ben-Yoseph, E. 1999. Computer Modeling of Sucrose Crystallization during Drying of Thin Films. Ph.D. dissertation, Univ. of Wisconsin, Madison.

Bibbs, D.G. 1995. Characterization of Flow and Packing Structure in Porous Media Using NMR Imaging. M.S. dissertation, Univ. of California, Davis. 123p.

Bikram, K. 1998. Rheological Properties of Starch in Aqueous Dimethylsulfoxide. MS Thesis, Univ. of Minnesota.

Bircan, Cavit. 1997. Effect of Viscosity on Dielectric Properties in Salty and Nonsalty Food Systems. MS Thesis, Ohio State Univ.

Bricknell, J.P. 1997. Bloom Inhibition in Dark Chocolate Using Milk Fat Fractions. MS Thesis, Univ. of Wisconsin-Madison.

Briggs, J.L. 1995. Methods to Characterize Power Law Fluids Using a Brookfield Viscometer. MS Thesis, Michigan State Univ. 143 p.

Buseman, G. 1996. Distribution oflsoflavones and Coumestrol in Fermented Miso and Edible Soybean Sprouts. MS Thesis, Iowa State Univ. 112 p.

Campos, D.T. 1996. Rheology of Developed and Undeveloped Wheat Flour Dough. Ph.D. dissertation, Michigan State Univ., 173 p.

Castelo, M. 1999.Stability of Mycotoxins in Thermally Processed Corn Products. Ph.D. dissertation, Univ. of Nebraska.

Chamberlain, E. K. 1996. Characterization of Heated and Thermally Processed Cross-Linked Waxy Maize Starch Utilizing Particle Size Analysis, Microscopy and
Rheology. MS Thesis, Comell Univ., Ithaca, NY.

Chamberlain, E. K. 1999. Rheological Properties ofAcid-Hydrolyzed Waxy Maize Starches. Ph.D. dissertation, Cornell Univ., Ithaca, NY.

Chamchong, M. 1997. Microwave Thawing of Foods: Effect of Power Levels, Dielectric Properties and Sample Geometry. Ph.D. Dissertation. Cornell Univerisity.

Chandra, M. Carbon Dioxide Hydration Using Carbonic Anhydrase Purified from Mammalian Blood, M.S. thesis, Purdue University, West Lafayette, IN.

Chang, Y-H. 1995. Freeze Concentrated Skim Milk: Ice Crystallization and Flow Properties. MS Thesis, Univ. of Wisconsin, Madison.

Chang, L. 1998. Physical, Mechanical, Thermal, and Viscoelastic Properties of Water-Blown Rigid Polyurethane Foam Containing Soy Flour. Ph.D. dissertation,
Univ. of Missouri-Columbia.

Chen, M. 1998. Puffing of Sorghum Cakes with a Rice Cake Machine. MS Thesis, Univ. of Missouri, Columbia.

Das, D. 997. Factors Effecting the Peelability of Tomatoes and Methods to Improve Chemical Peeling of Tomatoes. MS Thesis, Ohio State Univ.

Daubert,C.R. 1996. Electrorheology of Fluid Foods. Ph.D. dissertation, Michigan State Univ. 192 p.

Deng, Y. Estimation of Temperature Profiles in Microwaved Particulates Using Enzyme and Color Vision Systems, M.S. thesis, Purdue University, West Lafayette,
IN.

Erdogdu, F. 1996. Modeling of Temperature Distribution in Shrimp, and Measuring Its Effect on Texture, Shrinkage, and Yield Loss. MS Thesis, Univ. of Florida.
142p.

Faller, J.F. 1994. Die Design and Rheological Analysis in Twin-Screw Food Extrusion. Ph.D. dissertation, Univ. of Missouri, Columbia.

Fan, S. 1996. Puffing of Wheat Cakes Using a Rice Cake Machine. MS Thesis, Univ. of Missouri, Columbia.

Fonkwe, L. G. Production and Characterization of Proteins from Mechanically Deboned Turkey Residue, Ph. D. thesis, Purdue University, West Lafayette, IN.

Fu, J-T. 1998. Rheology of Sol-Gel and Gel-Sol Transition ofLow-Methoxyl Pectin + Ca 2+ Gels: The Effect of Sweeteners. Ph.D. dissertation, Cornell Univ.,
Ithaca, NY.

Gabarra, P. 1996. The Effects of Corn Syrup Solids and Their Oligosaccharide Fractions on the Glass Transition and Crystallization of Amorphous Sucrose. MS
Thesis, Univ. of Wisconsin, Madison.

Garber, B.W. 1995. The Influence of Particle Size on the Twin-Screw Extrusion of Corn Snacks. MS Thesis, Univ. of Missouri, Columbia.

Gunawan, M. I. 1998. Chlorophyll Degradation of Processed Broccoli during Refrigerated Storage. MS Thesis, Ohio State Univ.

Guo, Z. 1998. Prediction of Corn Tortilla Textural Quality Using Stress Relaxation Methods. MS Thesis, Texas A&M University. Hou, H. Pasteurization of Shell
Eggs for Salmonella Reduction, M.S. thesis, Purdue University, West Lafayette, IN.

Jauhari, P. 1997. A Study of the Diffusion of Bovine Serum Albumin at the Oil-Water Interface Using Total Internal Reflection Fluorescence and Fluorescence
Photobleaching Recovery. MS Thesis, Department of Chemical Engineering, Michigan State Univ.

Johnson, J.M. 1998. Enzymatic Modification of Milk Fat. Ph.D. dissertation, Univ. of Wisconsin, Madison.

Khan, M. 1996. Modeling of Extrusion Cooking of Full-Fat Soybean in a Single Screw Extruder. Ph.D. dissertation, Univ. of Missouri, Columbia.

Kistler, A.H. 1996. Puffed Rice and Corn Cakes: Modeling Physical Characteristics and Fortified Antioxidant Vitamin Degradation. MS Thesis, Univ. of Missouri,
Columbia.

Kloeppel, K.M. 1998. Puffing of White and Yellow Dent Corn Cakes. MS Thesis, Univ. of Missouri, Columbia

Kollengode, A. 1996.Flavor Retention Enhancement in Extrudates by Internal Application Techniques. Ph.D. dissertation, Univ. of Nebraska. Li, A. 1997.
Dielectrics of Commonly Microwaveable Foods and Their Water-Salt Relationships. MS Thesis, Ohio State Univ.

Li, Y. 1994. Modeling of a Fully-Wiped Co-Rotating Twin-Screw Extruder. Ph.D. dissertation, Univ. of Missouri, Columbia.

Liao, H-J. 1998. Simulation of Continuous Sterilization of Fluid Food Products: The Role of Thermorheological Behavior of Starch Dispersion and Process
Optimization. Ph.D. dissertation, Cornell Univ., Ithaca, NY.

Lima, E. 1995. Formation of Resistant Starch Using Twin-Screw Extrusion Technology. MS Thesis, Univ. of Missouri, Columbia.

Lin, S. 1994. Utilization of Beef Tallow in the Production of Extruded Dry Pet Food. Ph.D. dissertation, Univ. of Missouri, Columbia. Lin, S. 1998. Meat Analog
Development and Physical, Chemical, and Sensory Properties. Ph.D. dissertation, Univ. of Missouri, Columbia.

Lin, Y. 1994. Biomass Based and Extended Plastic Foams. Ph.D. dissertation, Univ. of Missouri, Columbia.

Liu, Y. 1998. Development ofOat-Com Puffs with a Twin-Screw Extruder. MS Thesis, Univ. of Missouri, Columbia.

Livney-Miller, T. 1995. Effects of Sweetener and Stabilizer on Recrystallization in Ice Cream. MS Thesis, Univ. of Wisconsin, Madison.

Lobo, S. 1996. Characterization of Spatial Non-Uniformity in the Microwave Reheating of High Loss Foods. M.S. Thesis. Comell University.

Lu, W. 1997. Rigid Polyurethane Foams Extended with Biomass. MS Thesis, Univ. of Missouri, Columbia.

Luzuriaga, D. 1995. Development and Testing of an Automated Quality Evaluation Device for Shrimp. MS Thesis, Univ. of Florida. 189 p.

Matthey, F. 1996.Physical and Macromolecular Properties of Twin-Screw Extruded Corn Starch-Whey Protein Concentrate Blends. MS Thesis, Univ. of
Nebraska.

Metin, S. 1996. Crystallization Behavior and Kinetics of Blends of Cocoa Butter and Milk Fat or Milk Fat Fractions. Ph.D. dissertation, Univ. of Wisconsin,
Madison.

Miranda-Lopez, R. 1999. Effects of some Anti-staling Additives, pH and Storage on the Staling of Corn Tortillas. Ph.D. Dissertation, Texas A&M University.

Moody, Vertigo. 1997. Estimating Thermal Inactivation Kinetics of Microorganisms from a Continuous Dynamic Thermal Treatment Process. MS Thesis, Univ. of
Florida. 103 p.

Ni, H. 1997. Multiphase moisture transport in porous media under intensive microwave heating. Ph.D. Dissertation. Comell University.

Okan, E. Reducing Oil Uptake in Tortilla Chips by Carboxy-Methyl cellulose Addition and/or Baking, M.S. thesis, Purdue University, West Lafayette, IN.

Ou-Yang, F. Self-Learning Neural-Fuzzy Control System and its Application on HTST Heating in Aseptic Processing, Ph.D. thesis, Purdue University, West
Lafayette, IN.

Pandrangi, S. 1998. Treatment of Tomato Industry Effluent by Coagulation Using Ferric Chloride and Factors Affecting Peelability. MS Thesis, Ohio State Univ.

Parsons, M.H. 1994. Effects of Sodium Bicarbonate/SALP and Process Variables on Corn Meal Extrudates. MS Thesis, Univ. of Missouri, Columbia.

Patience, D.B. 1996. Melt Crystallization Kinetics and Pressure Filtration of Anhydrous Milk Fat. MS Thesis, Univ. of Wisconsin, Madison.

Pomchaloempong, P. 1999. Numerical Simulation, Validation, and Optimization of Nutrient Retention in Thermal Processing of Conduction Heated Foods in
Odd-Shaped Containers. Ph.D. dissertation, Univ. of Florida. 239p.

Ransom-Painter, K. 1995. Incorporation of Milk Fat, Milk Fat Fractions, and Cocoa Butter into Palm Kernel Oil Based Compound Coatings. MS Thesis, Univ. of
Wisconsin, Madison.

Rayas, L.M. 1995. Development and Characterization of Edible and/or Degradable Films from Wheat Proteins. Ph.D. dissertation, Michigan State Univ., 187 p.

Rocha-Herrera, A.R. 1997. Influence of Solvent Extraction, Maturity Stage, and Thermal Treatment on the Determination ofCapsaicin in Capsicums (Capsicum
annuum Spp.) and Their Products. Ph.D. dissertation, Iowa State Univ. 161p.

Rodenbush, C.M. 1999. Physical Properties of Fatty Acids and Vegetable Oils. MS Thesis, Univ. of Missouri, Columbia.

Roife, L.A. 1998. The Effect of Screw Speed, Moisture Content, and Particle Size on the Floatability, Durability, and Water Stability of Catfish Feed. MS Thesis,
Univ. of Missouri, Columbia.

Sadikin, S. 1999. Viscometric Measurement by Nuclear Magnetic Resonance Imaging. M.S. Thesis, Univ. of California, Davis. 208p.

Schluentz, E.J. 1997. Rheological Behavior and Microstructure of Developed and Undeveloped Wheat Dough. MS Thesis, Michigan State Univ. 155 p.

Schmelzer, J. 1998. Interactions of Milk Fat and Milk Fat Fractions with Confectionery Fats. MS Thesis, Univ. of Wisconsin, Madison. Shi, X. 1997.
Thermomechanics of Fracture in Freezing ofBiomaterials. Ph.D. Dissertation. Cornell University.

Shukia, B. 1998. Kinetics ofDesorption of Bovine Serum Albumin at the Oil-Water Interface Using Total Internal Reflection Fluorescence and Fluorescence
Photobleaching Recovery. MS Thesis, Department of Chemical Engineering, Michigan State Univ. (1998).

Son, S. Aseptic Processing of Non-Newtonian Fluids under Turbulent Flow Conditions, Ph. D. thesis, Purdue University, West Lafayette, IN.

Sun, H. 1996. Extraction and Fractionation of Amaranth Seed Oil. Ph.D. dissertation. North Dakota State Univ. 165 p.

Shen, C. 1996. Utilization of Dried Tofa to Improve Sensory and other Properties of Beef Patties. MS Thesis, Iowa State Univ. 80p.

Tang, C. 1996. Effects of Wheat Proteins and an Emulsifier on Spaghetti Processing and Qualities. MS Thesis, Univ. of Missouri, Columbia.

Tang, C. 1997. Multivariate Analysis of Physical Characteristics, Sensory Perception and Consumer Preference of Wheat Noodles. MS Thesis, Univ. of Missouri,
Columbia.

Tattiyakul, J. 1997. Studies on Granule Growth Kinetics and Characteristics of Tapioca Starch Dispersion during Gelatinization Using Particle Size Analysis and
Rheological Methods. MS Thesis, Cornell Univ., Ithaca, NY.

Tietz, R.A. 1998. The Effects of Milk Fat Minor Lipids on the Crystallization of Milk Fat Cocoa Butter Blends and Bloom Formation in Chocolate. MS Thesis,
Univ. of Wisconsin, Madison.

Wang, S-T. 1996. The Freezing Behavior of Water as Influenced by Ice Cream Stabilizers. Ph.D. dissertation, Ohio State Univ.

Wang, J. 1997. Continuous, Countercurrent Extraction of Pectin from Sunflower Heads. MS Thesis. North Dakota State Univ. 122 p.

Wang, Y. 1994. Extruded Packaging Foam Using Corn Starch and Isolated Soy Protein. MS Thesis, Univ. of Missouri, Columbia.

Welt, B. A. 1996. Kinetic Parameter Estimation in Prepackaged Foods Subjected to Dynamic Thermal Treatments. Ph.D. dissertation, Univ. of Florida. 214 p.

Williams, S. 1996. Phase Behavior of Mixtures of Palm Kernel Oil with Cocoa Butter, Milk Fat and Milk Fat Fractions. MS Thesis, Univ. of Wisconsin, Madison.

Wang, L. 1998. The Antioxidant Properties ofLycopene and Oxygenated Lycopene Derivatives. MS Thesis, Iowa State Univ. 127 p.

Wang, W. 1998. Identification of CCPs in Pork Slaughter Establishments Based on Microbiological Contamination on Carcasses. MS Thesis, Iowa State Univ. 68
p.

Wei, S. 1998. An Investigation of the Physicochemical Properties of Chlorinated Flour. MS Thesis, Department of Food Science and Human Nutrition, Michigan
State Univ. Xie, W. 1999. Numerical Analysis on Corn Flour Melt in Extruder Die and Extrusion of Corn Puffs with Wheat Starches. Ph.D. dissertation, Univ. of
Missouri, Columbia.

Xu, M.I 995. Countercurrent Washing of Sunflower Heads prior to Pectin Extraction. MS Thesis. North Dakota State Univ. 121 p.

Yang, W. H. 1997. Rheological Behavior and Heat Transfer to a Canned Starch Dispersion: Computer Simulation and Experiment. Ph.D. dissertation, Cornell
Univ., Ithaca, NY. Zhang, D. 1996. Numerical Simulation of Entry Flows of Corn Meal. Plan B MS Thesis, Univ. of Minnesota.

Zhang, H. 1999. Electromagnetic and Thermal Studies of Microwave Processing of Foods. Ph.D. Dissertation. Comell University.

PATENTS

Flugstad, B., E. Kolbe, J.W. Park, J.H. Wells, Y. Zhao. Capacitive dielectric heating system for pasteurization, sterilization and thawing of foods. U.S. Provisional
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Swartzel, K.R. and Simunovic, J. 1998. Nondestructive Method and System for Detection of Non-Uniformities in Hermetically Packaged Foods NCSU Ref.
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Swartzel, K.R. and Simunovic, J. 1999. Meth. and Sys. for Res. Time Meas. Of Sim. Fd. Par. in Cont. Ther. Fd Proc. and Sim. Fd Part. for Use in Same. US
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No. 5,549,041

APPENDIX B

UNIQUE STATION CAPABILITIES AVAILABLE FOR

COLLABORATIVE PROJECTS

California

Dynamic Solid Analyzer.. Rheometrics

Differential Scanning Calorimeter .. Perkin Elmer

Video microscope 50X ... Olympus

Walk-in Freezer with wind tunnel

GC and HPLC ... HP and Waters

Florida

Fully-equipped semi-works citrus packing and processing pilot plant

State-of-the-art rotary retort, with full control capabilities

Closing machines for cans, glass, pouches, and semi-rigid containers

Facilities for research and testing of modified atmosphere packaging

Ultra-high pressure unit, 2.4 It capacity, -20 to 90C

Expertise in software development, especially in thermal processing

National high magnetic field lab

Food and Drug Administration

UV light reactor for juice processing.

Continuous unit is expected to be ready by FYOO. I

llinois (National Center for Food Safety and Technology)

Pilot scale Batch high pressure food processor

Pilot scale semi-continuous high pressure food processor

Laboratory scale pulsed electric field food processor

Equipment for determining thermal, physical & electrical properties of foods

Ozone processing system

NCFST is also in the process of installing a pilot scale aseptic processing system

Indiana

Aseptic packaging machine (Metal Box, single lane)

Supercritical Fluid Extractor (Isco)

Q-Test Texture Analyzer

Differential Scanning Calorimeter

NMR machines

Iowa

Linear Accelerator Facility - irradiation

High Pressure processing system

Soybean/soyfood commercial (Japanese system) processing pilot plant

Aroma/flavor/sensory testing equipment and human panelists (prob. similar to other stations Electronic Nose, GC, etc.)

Isoflavone analysis (samples sent here from all over the world)

Oil extraction from soybeans and oil seeds Haake and other rheological equipment

Michigan

Assessment of the interfacial behavior of biological macromolecules, particularly proteins

Acquiring and interpreting surface/interfacial tension data

Complete rheological analysis of fluid foods

Missouri

RheoStress RS100 (Haake, Paramus, NJ). A sophisticate rheometer which allows rheological measurements under controlled stress (CS), controlled rate (CR) and
oscillation (OSC) test modes.

Exstar 6100 Dynamic Mechanical Thermal analyzer (Seiko Instruments, Chiba, Japan). This instrument has four modes of sample deformation including
compression, tension, shear and bending, and is able to operate from -150 to 600C at 0.01 to 20C/min heating and cooling rate from 0.01 to lOOHz. It also has
Fourier transform technology in the noise reduction, and is able to handle a wide range of materials from solid films to melts.

The Pyris 1 Differential Scanning Calorimetry with TAC 7/PC Thermal Analysis Controller (Perkin-Elmer Corp., Norwalk, CT) is a state-of-the-art computer
controlled laboratory instrument that operates with Perkin-Elmer's unique power compensation design.

TA.XT2 Texture Analyzer with XTRA Dimension software (Texture Technologies Corp., Scarsdale, NY). It provides force or distance measurements in
compression or tension mode with a wide variety of available probes.

The Fox 200 heat flow meter instrument (LaserComp, Wakefield, MA). A complete system with thermal conductivity instrument for testing in accordance with
ASTM C518 and ISO 8301 specifications.

APV Baker 50/25 MPF intermeshing, co-rotating twin-screw extruder (APV Baker, Grand Rapids, MI). This extruder is a pilot plant model and is similar to but
more versatile than commercial extruders. Materials are conveyed along an enclosed barrel where they are subjected to a combination of heating, cooling, mixing
and shear. The screws can be built in any number of configurations using five types of screw element. Maximum screw speed is 500 rev/min. The processing
chamber (barrel) has a length to diameter ratio (L/D) of 25:1 and splits along the horizontal axis for easy cleaning. The barrel diameter is 50 mm. The barrel is heated
and cooled in zones. Each heating/cooling zone is 2.5 D long and has an independent temperature controller giving heating or cooling as required on a time
proportional basis. The feed port is provided with a detachable feed chute and accepts feed from a K-tron twin-screw volumetric feeder. A liquid feed port is
provided in each zone. These ports can also be used for measurement of product temperature or pressure using industry standard probes. The main drive power (28
kW) is provided by a silicon controlled rectifier, direct current drive. The motor is coupled via a mechanical torque limit device to a splitter/reduction gearbox to
drive the twin output shafts. A rigid box frame carries all the components of the extruder.

Nebraska

C.W. Brabender Extruders - single and twin screw, mixing and non mixing configurations, and film blowing and compounding capabilities.

Permeability measurement of thin films - CO 2 and H:20

New Jersey

Laser Doppler Anemometer applications in extrusion

Jet impingement heat transfer applications to baking

Mechanical dynamic measurements of glass transition temperature

Intelligent microwave oven for more precise control of product residence time

FIDAP and FLUENT software for simulation of heat and mass transfer

Numerical simulation ofviscoelastic flows

New York (Geneva)

Isothermal Heating Apparatus (John Roberts).

This heating equipment incorporates a multi-mode microwave oven with Variable continuous power and a feedback temperature controller for rapid internal heating
along with variable convective hot air for rapid surface heating. Utilizing these two heating mechanisms in a controlled system, the operator is able to heat food
particulates below boiling temperatures isothermally and obtain desired temperatures within seconds.

Temperature Data Acquisition in a Microwave Oven (John Roberts). This data acquisition is an eight channel fiber-optic system that is able to record
time-temperature measurements in a microwave environment. There are many systems similar to this, but the uniqueness of this system is that it is attached to the
rotating glass tray in a home microwave oven and the unit rotates with the product on a slip-ring device. Thus temperature profiles can be obtained in food products
as they heat and rotate in a home microwave oven.

AR 100 Rheometer, TA Instruments (Andy Rao) With this rheometer, one can conduct flow, creep, and dynamic rheological tests, as well as measure normal
stresses of fluid and semisolid foods. The Peltier temperature control system can control the temperature of a test sample between -20 to 180°C.

Dynamic Mechanical Analyzer (DMA), Model 2980, TA Instruments (Andy Rao)

The DMA should allow us to study the rheological properties of solid foods. We plan to use for studies on fruits and vegetables.

Fruit and Vegetable Processing Pilot Plant (Department ofFS&T)

The pilot plant is dedicated to processing of fruits and vegetables. It is used to support food processors interested in production, pasteurization, and concentration of
fruit juices, and canning of vegetables.

New-York (Ithaca)

Software, hardware and trained personnel for computational modeling in heat transfer, mass transfer, thermo- and hygromechanics and coupled
thermal-electromagnetics. Software includes commercial ones such as FIDAP and FLUENT as well as home grown ones. The applications in the past have been to
cracking during rapid freezing, electromagnetic field patterns in microwave heating, and heat and moisture transfer in microwave heating, infrared heating, baking and
frying.

Laboratory microwave oven with instrumentation to measure forward and reflected power and with mode stirrer to improve uniformity.

Fiberoptic temperature and pressure measurement system that is immune to electromagnetic interference, as in a microwave oven.

North Carolina

Continuous flow radio frequency unit 30 kW, 40.68 MHz

Manufacturer: Radio Frequency Co., Inc., Millis, MA

Applications: Uniform heating of viscous and particulate products

Software: CFD-ACE+ Vendor: CFD Research Corp., Huntsville, AL; Applications: Modeling fluid flow, heat transfer (includes grid generation and post-processing
also. Has capability to incorporate use defined subroutines)

Single and Multicoil heat exchangers Vendor: VRC Co., Cedar Rapids, IA Applications: Rapid and uniform heating (ultrapasteurization) ; minimum to no fouling
Bohlin VOR controlled-strain rheometer

Haake VT-550 Viscotester

StressTech controlled stress rheometer with sealed cell attachment for couette geometry allows measurement of viscosity at temperatures higher than 100 °C

Electrorheological attachment for Haake VT550

MTS/histron Universal Testing machine

Differential Scanning Calorimeter, Perkin Elmer DSC 7 with modulated capability (Pyris 1) Dynamic Mechanical Analysis, Perkin Elmer

Micromeritics Helium Pycnometer: Determination of true and bulk particle density and porosity

International Paper SA-50 Aseptic Filler ( 250 ml aseptic brick packs at 275 gal/hr with a minimum batch size of 100 gal; 3600 pkg/hr; single cycle: unfolded
pouches with a minimum batch size of 5 gal.)

Scholle 9-S auto-fill, extended life, bag-in-box filler; 1 - 3 gal; SchoUe Cheny Buirell EQ-3 ESL clean-fill filler (8, 16, 32 ounces; 26 - 70 units/min; half pint, quart
gable-top containers),

Cherry-Burrell, Cedar Rapids, IA.

North Dakota

Bench-scale solvent extraction

Mini expeller and other oilseed processing

Tofu/soy milk pilot plant

Ohio

PEF pilot facility with aseptic packaging

Ohmic heating pilot facility

High Pressure Processing facility

Continuous flow microwave processing units

Ozonation equipment

A high speed microscopic imaging system for imaging bacterial cells during PEF treatment.

Liquid crystal/image analysis temperature measurement

Particle tracking velocimetry capability for measurement of interstitial velocity and solids motion in multiphase flow.

PEF bacterial death kinetics equipment

Ohio Supercomputer Center, with various CFD and other computational codes.

Pennsylvania

Characterization of dielectric properties of food systems: Network analyzer, coaxial probe, transmission cell

Characterization of gas permeabilities of food packaging systems:

MOCON/Oxygen transmission rate measurement system, Permatran/Water vapor transmission rate measurement system

Continuously-variable-power microwave oven and fluoroptic temperature measurement system.

Texas

Snacks processing lab - tortilla chips processing

Rheological measurements lab (controlled stress rheometer, 2 Haakes, 3 Brookfields, 2 Texture Analyzers)

Vaccum and pressure frying units, permeability probe of porous media

Impingement drying (steam and air)

Extrusion (twin and single screw), reverse osmosis and ultrafiltration (membranes)

Washington

High Pressure Press

Wisconsin

Dynamic Mechanical Analysis (DMA): Perkin Elmer

Differential Scanning Calorimeter (DSC): Perkin Elmer DSC 7 and Perkin Elmer Pyris 1 with modulated capability

Submersible Microscope Probe: Lasentec PVM

Automated Image Analysis system: Nikon Labophot and Optiphot microscopes and Optimas 6.1 image analysis software

Refrigerated glove box (home made) for work on frozen foods

RELATED CURRENT AND PREVIOUS WORK

The following projects were identified through a search of the CRIS (U.S.) and ICAR (Canada) databases:

Projects involving NC-136 members:

Project Number: CA-D*-AER-3499-RR Performing Organization: AGRI ENGINEERING Performing Institution: UNIV OF CALIFORNIA Investigator(s):
SINGH R P Project Title- IMPROVEMENT OF THERMAL PROCESSES FOR FOODS.

Project Number: CA-D*-FST-5641-RR Performing Organization: FOOD SCIENCE AND TECHNOLOGY Performing Institution: UNIV OF CALIFORNIA
Investigators)- MCCARTHY M J MCCARTHY K L Project Title: IMPROVEMENT OF THERMAL PROCESSES FOR FOODS.

Project Number: FLA-AGE-03456 Performing Organization: AGRI ENGINEERING Performing Institution: UNIVERSITY OF FLORIDA Investigators):
TEDCEIRA A A SMERAGE G H Project Title: IMPROVEMENT OF THERMAL PROCESSES FOR FOODS.

Project Number: ILLW-NC-136 Performing Organization: NATIONAL CNTR FOR FOOD SAFETY Performing Institution: ILLINOIS INSTITUTE OF
TECHNOLOGY Investigators)- BALASUBRAMANIAM VM Project Title: IMPROVEMENT OF THERMAL PROCESSING FOR FOODS.

Project Number: ILLR-9603758 Performing Organization: NATL CENTER FOR FOOD SAFETY & Performing Institution: ILLINOIS INSTITUTE OF
TECHNOLOGY Investigator(s): BALASUBRAMANIAM JM Project Title: ELECTRICAL RESISTANCE HEATING OF MULTIPHASE FOODS.

Project Number: ILLU-69-0201 Performing Organization: UNIVERSITY ADMINISTRATION Performing Institution: UNIVERSITY OF ILLINOIS
Investigator(s): BALASUBRAMANIAM V PALANIAPPAN S REDDY R Project Title: HIGH ISOSTATIC PRESSURE INACTIVATION OF SELECTED
FOOD SPOILAGE MICRORGANISMS .

Project Number: IND060017A Performing Organization: FOOD SCIENCE Performing Institution: PURDUE UNIVERSITY Investigator(s): MARKS J S Project
Title- IMPROVEMENT OF THERMAL PROCESSES FOR FOODS.

Project Number: IOW02164 Performing Organization: FOOD TECHNOLOGY Performing Institution: IOWA STATE UNIVERSITY Investigator(s): WILSON
L A NIKOLOV Z L MURPHY P A Project Title: IMPROVEMENT OF THERMAL PROCESSES FOR FOODS.

Project Number: MIN-12-030 Performing Organization: AGRI ENGINEERING Performing Institution: UNIV OF MINNESOTA Investigator(s):
BHATTACHARYA M K APOOR B Project Title: IMPROVEMENT OF THERMAL PROCESSES FOR FOODS.

Project Number: NC00836 Performing Organization: FOOD SCIENCE Performing Institution: NORTH CAROLINA STATE UNIV Investigators): FARKAS B
E SWARTZEL K R Project Title: IMPROVEMENT OF THERMAL PROCESSES FOR FOODS .

Project Number: NC05483 Performing Organization: FOOD SCIENCE Performing Institution: NORTH CAROLINA STATE UNIV Investigator(s): DAUBERT
C R Project Title: RHEOLOGICAL PROPERTIES OF FOOD AND BIOLOGICAL SYSTEMS.

Project Number: NC05859 Performing Organization: FOOD SCIENCE Performing Institution: NORTH CAROLINA STATE UNIV Investigator(s): SANDEEP
K P SWARTZEL K R Project Title: ENGINEERING STUDIES ON CONTINUOUS FLOW THERMAL PROCESSES FOR FLUID FOODS .

Project Number: NC06393 Performing Organization: FOOD SCIENCE Performing Institution: NORTH CAROLINA STATE UNIV Investigators): FARKAS BE
Project Title: PHASE CHANGE AND MOVING BOUNDARY PROBLEMS IN FOOD PROCESSING OPERATIONS.

Project Number: NC06482 Performing Organization: FOOD SCIENCE Performing Institution: NORTH CAROLINA STATE UNIV Investigators): KEENER
KM Project Title: TRANSPORT PHENOMENA IN AGRICULTURAL AND BIOLOGICAL PROCESSES.

Project Number: ND01452 Performing Organization: AGRI ENGINEERING Performing Institution: NORTH DAKOTA STATE UNIV Investigator(s):
WIESENBORN D P Project Title: IMPROVEMENT OF THERMAL PROCESSES FOR FOODS.

Project Number: NEB-11-044 Performing Organization: BIOLOGICAL SYSTEMS ENGINEERING Performing Institution: UNIVERSITY OF NEBRASKA
Investigator(s): HANNA M A CHINNASWAMY R Project Title: IMPROVEMENT OF THERMAL PROCESSES FOR FOODS .

Project Number: NYG623493 Performing Organization: FOOD SCIENCE AND TECHNOLOGY Performing Institution: N Y AGRICULTURE EXPT
STATION Investigator(s): RAO M A WALTER R H Project Title: IMPROVEMENT OF THERMAL PROCESSES FOR FOODS.

Project Number: NYG623560 Performing Organization: FOOD SCIENCE AND TECHNOLOGY Performing Institution: N Y AGRICULTURE EXPT
STATION Investigator(s): RAO MA WALKER LP Project Title: ROLE OF GRANULE SIZE AND VISCOMETER GEOMETRY IN RHEQLOGY OF
STARCH DISPERSIONS.

Project Number: OH000768-SS Performing Organization: AGRI ENGINEERING Performing Institution: OHIO STATE UNIV Investigator(s): SASTRY S K
Project Title: OHMIC HEATING AND RAPID COOLING OF SOLID-LIQUID MDCTURES.

Project Number: TEX03366 Performing Organization: AGRI ENGINEERING Performing Institution: TEXAS A&M UNIV Investigator(s): MOREIRA R G
LACEY R E SWEAT V E Project Title: IMPROVEMENT OF THERMAL PROCESSES FOR FOODS.

Project Number: WNP00223 Performing Organization: BIOLOGICAL SYSTEMS ENGINEERING Performing Institution: WASHINGTON STATE
UNIVERSITY Investigators): TANG J CAVALIERI R P PITTS M J Project Title: APPLICATION OF MICROWAVE HEATING IN FOOD AND
AGRICULTURE PROCESSES . Other related U.S. Projects:

Project Number: 6612-41420-003-OOD Performing Institution: AGRICULTURAL RESEARCH SERVICE Investigators): DICKENS J A CASON JR J A
BUHR R J Project Title: ENGINEERING INNOVATIONS AND MICRO DEVELOPMENTS TO REDUCE CONTAMINATIO N OF POULTRY AND
EQUIPMENT.

Project Number: 1935-41420-001-OOD Performing Organization: AGRICULTURAL RESEARCH SERVICE Performing Institution: EASTERN REGIONAL
RES CENTER Investigator(s): MORGAN A I GOLDBERG N M Project Title: DESIGN OF PROTOTYPE SURFACE PASTEURIZER FOR FRESH MEATS
AND POULTRY.

Project Number: ARK01677 Performing Organization: BIOLOGICAL & AGR ENGINEERING Performing Institution: UNIVERSITY OF ARKANSAS
Investigator(s): MARKS B P MARCY J A SIEBENMORGEN T J Project Title: QUANTIFYING THE DEGREE OF COOKING FOR
FURTHER-PROCESSED POULTRY PRODUCTS.

Project Number: CA-D*-FST-6462-H Performing Organization: FOOD SCIENCE AND TECHNOLOGY Performing Institution: UNIV OF CALIFORNIA
Investigators): SHOEMAKERCF Project Title: THE EFFECT OF FOOD POLYMER COMPOSITION AND STRUCTURE ON THE RHEOLOGY AND
TEXTURE OFFOODS .

Project Number: GE001500 Performing Organization: FOOD SCIENCE AND TECHNOLOGY Performing Institution: UNIVERSITY OF GEORGIA
Investigator(s): HUNG Y C Project Title- VALUE-ADDED PROCESSES TO ENHANCE THE QUALITY AND SAFETY OF FOODS.

Project Number: IND046058 Performing Organization: AGRI ENGINEERING Performing Institution: PURDUE UNIVERSITY Investigator(s): HAGHIGHI K
Project Title- APPLICATION OF FINITE ELEMENT TO PRODUCTION AND PROCESSING OF FOOD AGR. AND BIOLOGICAL MATERIALS .

Project Number: MAS-9502429 Performing Organization: FOOD SCIENCE Performing Institution: UNIV OF MASSACHUSETTS Investigator(s): PELEG M
Project Title- IMPERFECT SQUEEZING FLOW VISCOSIMETRY FOR FOOD PRODUCTS.

: MAS09701494 Performing Organization: FOOD SCIENCE Performing Institution: UNIV OF MASSACHUSETTS Investigator(s): MCCLEMENTS D J
Project Title- NON-DESTRUCTIVE CHARACTERIZATION OF FOOD EMULSIONS USING ULTRASOUND.

Project Number: NYG623559 Performing Organization: FOOD SCIENCE AND TECHNOLOGY Performing Institution: N Y AGRICULTURE EXPT
STATION Investigator(s): SPLITTSTOESSER D P MCLELLAN M R Project Title: PASTEURIZATION PROCESSES FOR THE DESTRUCTION OF
ESCHERICHIA COLI 0157:H7 IN SWEET CIDER. P

Project Number: TEN00125 Performing Organization: FOOD SCIENCE AND TECHNOLOGY Performing Institution: UNIVERSITY OF TENNESSEE
Investigator(s): HULBERT G J RAMAN R WILHELM L Project Title: ENGINEERING SYSTEMS FOR VALUE-ADDED FOOD PROCESSING AND
WASTE UTILIZATION.

Project Number: UTA00226 Performing Organization: NUTRITION & FOOD SCIENCE Performing Institution: UTAH STATE UNIVERSITY Investigator(s):
MCMAHON D IRUDAYARAJ J Project Title: EVALUATION OF ELECTROHEATING TECHNOLOGY FOR UHT PROCESSING OF MILK.

Project Number: VA-135503 Performing Organization: FOOD SCIENCE AND TECHNOLOGY Performing Institution: VIRGINIA POLYTECHNIC
INSTITUTE Investigators): PffiRSON M D Project Title: DESTRUCTION OF CLOSTRIDIUM BOTULINUM IN FOODS AT MINIMAL PROCESSING
TEMPERATURES .

Project Number: 5325-42000-024-OOD Performing Institution: WESTERN REGIONAL RES CENTER Investigators): TSAI L S HERNLEM B J
ROBERTSON G H Project Title: ADV. TECHNOLOGIES FOR REDUCTION OF MICROORGANISMS AND PARTICULATE MATTER IN FOOD
PROCESSING .

Project Number: WIS04015 Performing Organization: BIOLOGICAL SYSTEMS ENGINEERING Performing Institution: UNIV OF WISCONSIN
Investigator(s): GUNASEKARAN S Project Title: RHEOLOGICAL PROPERTIES OF BIOPOLYMER GEL SYSTEMS.

Related Canadian Research Projects

Project Number: 333-1411-9611 AGRICULTURE AND AGRI-FOOD CANADA RESEARCH BRANCH FOOD RESEARCH AND DEVELOPMENT
CENTREPASSEY C A Development of separation and fractionation technologies for value-added processing of milkfat.

Project Number: 11680 Performing Organization: UNIVERSITY OF GUELPH, COLLEGE OF PHYSICAL AND ENGINEERING SCIENCES Investigator(s):
BROWN R TECH Project Title: Digital image analysis and interpretation in food processing and grading systems.

Project Number: 11270 Performing Organization: UNIVERSITY OF GUELPH, ONTARIO AGRICULTURAL COLLEGE Investigators): TUNG M TECH
Project Title: Temperature controlled food packaging for improved shelf life, quality and safety.

Project Number: 16430 Performing Organization: UNIVERSITY OF GUELPH, ONTARIO AGRICULTURAL COLLEGE Investigators): MCKNIGHT D
TECH Project Title: Sanitizing milk lines and milk handling equipment with special references to rubber hoses, gaskets and inflations.

Project Number: AGENG022 UNIVERSITY OF MANITOBA FACULTY OF AGRICULTURAL AND FOOD SCIENCES JAYAS D S Optimization of
canned food sterilization and measurement of thermal properties of irregular shaped food materials.

Project Number: 11430 Performing Organization: UNIVERSITY OF GUELPH COLLEGE OF PHYSICAL AND ENGINEERING SCIENCES Investigators).•
MITTAL G TECH Project Title: To investigate the mechanisms of food frying processes for lower fat and better quality products. Performing Organization:
MACDONALD CAMPUS OF MCGILL UNIVERSITY FACULTY OF AGRICULTURAL AND ENVIRONMENTAL SCIENCES Performing Institution:
21-111 Lakeshore Road Investigators): RAMASWAMY H SABLANI S Project Title: Quality enhancement of foods through rotational processing. Performing
Organization: MACDONALD CAMPUS OF MCGILL UNIVERSITY FACULTY OF AGRICULTURAL AND ENVIRONMENTAL SCIENCES Performing
Institution: 21-111 Lakeshore Road Investigators): RAMASWAMY H GRABOWSKI S TAJCHAVAVIT S Project Title: Heat transfer techniques for improved
food processing.

Project Number: 333-1421-9307 Performing Organization: AGRICULTURE AND AGRI- FOOD CANADA RESEARCH BRANCH FOOD RESEARCH
AND DEVELOPMENT CENTRE Performing Institution: 3600 Casavant Boulevard West Investigator(s): MARCOTTE M Project Title: Amelioration de la qualite
des aliments par Ie developpement ou la mise au point de traitements thermiques de stabilisation. 107