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Dense Phase Carbon Dioxide : Food and Pharmaceutical Applications.
Title:
Dense Phase Carbon Dioxide : Food and Pharmaceutical Applications.
Author:
Balaban, Murat O.
ISBN:
9781118243343
Personal Author:
Edition:
1st ed.
Physical Description:
1 online resource (336 pages)
Contents:
Dense Phase Carbon Dioxide: Food and Pharmaceutical Applications -- Contents -- Preface -- Contributors -- 1 Introduction to Dense Phase Carbon Dioxide Technology -- 2 Thermodynamics of Solutions of CO2 with Effects of Pressure and Temperature -- 2.1 Introduction -- 2.2 Thermodynamics of liquid-vapour phase equilibria -- 2.2.1 Calculation of γ -- 2.2.2 Calculation of Φ -- 2.2.3 Calculation of the liquid-vapour phase equilibria -- 2.3 Application to CO2-H2O system model -- 2.3.1 Non-electrolyte models -- 2.3.2 Electrolyte models -- 2.4 Thermodynamics of solid-vapour equilibria -- 2.5 List of symbols -- 3 Experimental Measurement of Carbon Dioxide Solubility -- 3.1 Introduction -- 3.2 Solubility of carbon dioxide in water -- 3.2.1 Definition and brief review of early studies -- 3.2.2 Physical properties associated with the phase diagram of carbon dioxide -- 3.2.3 Effect of pressure and temperature on carbon dioxide solubility in water -- 3.3 Experimental methods for carbon dioxide solubility measurement -- 3.3.1 Analytical methods -- 3.3.2 Synthetic methods -- 3.4 Review of experimental results -- 3.5 Conclusions -- 4 Effects of Dense Phase Carbon Dioxide on Vegetative Cells -- 4.1 Introduction -- 4.2 Gases used for inactivating microorganisms -- 4.3 Effect of DPCD on vegetative microorganisms -- 4.3.1 Effect of DPCD on bacterial cells -- 4.3.2 Effect of DPCD on vegetative forms of fungi, pests and viruses -- 4.4 Factors affecting the sensitivity of microorganisms to DPCD -- 4.4.1 Effect of CO2 physical states -- 4.4.2 Effect of temperature and pressure -- 4.4.3 Effect of CO2 concentration -- 4.4.4 Effect of agitation -- 4.4.5 Effect of water content -- 4.4.6 Effect of pressurization and depressurization rates -- 4.4.7 Effect of pressure cycling -- 4.4.8 Effect of microbial type -- 4.4.9 Effect of initial microbial number.

4.4.10 Effect of physical and chemical properties of suspension -- 4.4.11 Effect of culture conditions and growth phases -- 4.4.12 Injured microorganisms -- 4.4.13 Effect of combination processes -- 4.4.14 Effect of type of system -- 4.4.15 Treatment time and inactivation kinetics -- 4.5 Mechanisms of microbial inactivation by DPCD -- 4.5.1 Solubilization of CO2 under pressure into suspension -- 4.5.2 Cell membrane modification -- 4.5.3 Cytoplasmic leakage -- 4.5.4 Intracellular pH decrease -- 4.5.5 Key enzyme inactivation -- 4.5.6 Inhibitory effect of molecular CO2 and HCO3- on metabolism -- 4.5.7 Intracellular precipitation and electrolyte imbalance -- 4.5.8 Extraction of vital cellular constituents -- 4.5.9 Physical cell rupture -- 4.6 Characterization of CO2 states and survival curves -- 4.7 Quantifying inactivation -- 4.8 Conclusions -- 5 Effects of Dense Phase Carbon Dioxide on Bacterial and Fungal Spores -- 5.1 Introduction -- 5.2 Inactivation of bacterial spores by DPCD -- 5.2.1 Effect of temperature -- 5.2.2 Effect of pressure -- 5.2.3 Effect of pH and aw of the treatment medium -- 5.2.4 Susceptibility of different bacterial spores -- 5.2.5 Effects of combination treatments -- 5.2.6 Mechanisms of bacterial spore inactivation -- 5.3 Inactivation of fungal spores by DPCD -- 5.4 Conclusion -- 6 Effects of DPCD on Enzymes -- 6.1 Introduction -- 6.2 Effects of gas bubbling -- 6.3 Alteration of the protein structure -- 6.4 Studies with multiple enzymes -- 6.5 Effects on specific enzymes -- 6.5.1 Alpha-amylase -- 6.5.2 Acid protease -- 6.5.3 Alkaline protease -- 6.5.4 Gluco-amylase -- 6.5.5 Lipase -- 6.5.6 Pectinesterase (PE) -- 6.5.7 Pectin methyl esterase (PME) -- 6.5.8 Polyphenol oxidase (PPO) -- 6.5.9 Tyrosinase -- 6.5.10 Lipoxygenase -- 6.5.11 Peroxidase -- 6.5.12 Alkaline phosphatase -- 6.5.13 Myrosinase -- 6.5.14 Hydrolases.

6.6 Conclusions and suggestions -- 7 The Kinetics of Microbial Inactivation by Carbon Dioxide under High Pressure -- 7.1 Introduction -- 7.2 The survival curve -- 7.2.1 Primary models -- 7.2.2 Secondary models - the effect of pressure alone -- 7.2.3 The temperature effect and that of other auxiliary factors -- 7.2.4 Dynamic treatments -- 7.3 Application of the models to published experimental data -- 7.3.1 Primary model derivation -- 7.4 Concluding remarks -- 7.5 List of symbols -- 8 Applications of DPCD to Juices and Other Beverages -- 8.1 Introduction -- 8.2 Juices processed with DPCD -- 8.2.1 Orange juice -- 8.2.2 Apple juice -- 8.2.3 Mandarin juice -- 8.2.4 Grapefruit juice -- 8.2.5 Watermelon juice -- 8.2.6 Coconut water -- 8.2.7 Guava puree -- 8.2.8 Grape juice -- 8.2.9 Pear -- 8.2.10 Carrot -- 8.2.11 Carrot juice -- 8.2.12 Peach -- 8.2.13 Kiwi -- 8.2.14 Melon -- 8.3 Other beverages processed with DPCD -- 8.3.1 Beer -- 8.3.2 Kava kava -- 8.3.3 Jamaica beverage -- 8.4 Conclusions -- 9 Use of Dense Phase Carbon Dioxide in Dairy Processing -- 9.1 Introduction -- 9.2 Carbon dioxide in milk -- 9.3 Enzymes and microorganisms in milk -- 9.4 Application of carbon dioxide to milk -- 9.4.1 Carbon dioxide addition to raw milk -- 9.4.2 Carbon dioxide addition during thermal pasteurization of milk -- 9.4.3 Effect of carbon dioxide addition on sensory properties of milk -- 9.4.4 Dense phase carbon dioxide process -- 9.5 Application of carbon dioxide for enzyme inactivation -- 9.6 Application of carbon dioxide to cottage cheese production -- 9.7 Application of carbon dioxide to yogurt and fermented products -- 9.8 Application of carbon dioxide to casein production -- 9.8.1 Casein properties -- 9.8.2 Casein production by high-pressure carbon dioxide -- 9.8.3 Comparison between continuous and batch systems for casein production by carbon dioxide.

9.8.4 Economic comparison between high-pressure carbon dioxide and a conventional process for casein production -- 9.9 Conclusions -- 10 Particle Engineering by Dense Gas Technologies Applied to Pharmaceuticals -- 10.1 Introduction -- 10.2 Dense gas as a solvent -- 10.2.1 Rapid expansion of supercritical solutions -- 10.2.2 Rapid expansion of supercritical solutions with a solid solvent -- 10.2.3 Rapid expansion of supercritical solutions with a nonsolvent -- 10.2.4 Particles from gas-saturated solutions -- 10.3 Dense gases as antisolvents -- 10.3.1 Gas antisolvent process -- 10.3.2 Aerosol solvent extraction system -- 10.3.3 Solution-enhanced dispersion by supercritical fluids -- 10.3.4 Atomized rapid injection for solvent extraction -- 10.4 SCFs as co-solvents -- 10.4.1 Depressurisation of an expanded liquid organic solvent -- 10.5 Dense gases as aerosolisation aids (spray-drying assistance) -- 10.5.1 Carbon dioxide-assisted nebulisation with a bubble dryer -- 10.5.2 Supercritical fluid assisted atomisation -- 10.6 Conclusion -- 11 Industrial Applications Using Supercritical Carbon Dioxide for Food -- 11.1 Overview -- 11.2 Past development -- 11.3 Mechanism of microbial inactivation -- 11.3.1 Effect of other gases on microbial inactivation -- 11.4 scCO2 commercialization activities -- 11.5 Porocrit process -- 11.5.1 Impact on juice quality -- 11.5.2 Impact on nutrient values -- 11.5.3 Impact on microbial inactivation -- 11.5.4 Impact on microbial inactivation for solid foods -- 11.5.5 scCO2 processing efficiencies -- 11.6 Conclusions -- 12 Outlook and Unresolved Issues -- 12.1 Introduction -- 12.2 Unresolved issues -- 12.2.1 Inactivation mechanism of DPCD -- 12.2.2 Food quality and storage -- 12.2.3 Target foods -- 12.2.4 Process equipment and intellectual property -- 12.2.5 Fouling, cleaning, and disinfecting.

12.2.6 Occurrence of DPCD-resistant mutants -- 12.2.7 Industrial implementation and process economics -- 12.3 Future outlook and conclusions -- 12.4 Acknowledgements -- References -- Index.
Abstract:
Dense phase carbon dioxide (DPCD) is a non-thermal method for food and pharmaceutical processing that can ensure safe products with minimal nutrient loss and better preserved quality attributes. Its application is quite different than, for example, supercritical extraction with CO 2 where the typical solubility of materials in CO 2 is in the order of 1% and therefore requires large volumes of CO 2. In contrast, processing with DPCD requires much less CO 2 (between 5 to 8% CO 2 by weight) and the pressures used are at least one order of magnitude less than those typically used in ultra high pressure (UHP) processing. There is no noticeable temperature increase due to pressurization, and typical process temperatures are around 40°C. DPCD temporarily reduces the pH of liquid foods and because oxygen is removed from the environment, and because the temperature is not high during the short process time (typically about five minutes in continuous systems), nutrients, antioxidant activity, and vitamins are much better preserved than with thermal treatments. In pharmaceutical applications, DPCD facilitates the production of micronized powders of controlled particle size and distribution. Although the capital and operating costs are higher than that of thermal treatments, they are much lower than other non-thermal technology operations. This book is the first to bring together the significant amount of research into DPCD and highlight its effectiveness against microorganisms and enzymes as well as its potential in particle engineering. It is directed at food and pharmaceutical industry scientists and technologists working with DPCD and other traditional or non-thermal technologies that can potentially be used in conjunction with DPCD. It will also be of interest to packaging specialists and regulatory agencies.
Local Note:
Electronic reproduction. Ann Arbor, Michigan : ProQuest Ebook Central, 2017. Available via World Wide Web. Access may be limited to ProQuest Ebook Central affiliated libraries.
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