| C01 |
OPTIMIZATION OF SUBCRITICAL WATER – CARBON DIOXIDE SYSTEMS FOR THE EXTRACTION AND REACTIVE PROCESSING OF IORENEWABLE MATERIALS. |
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King J.-W., Zhang D., Srinivas K., Wang Y.-J. and Howard L., University of Arkansas,
Fayetteville (USA) |
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| C02 |
SUPERCRITICAL FLUID EXTRACTION OF Lippia Dulcis Trev. |
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Oliveira P.-F., Machado R.-A.-F and Bolzan A., Santa Catarina Federal University, Florianopolis (Brazil) |
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| C03 |
A GREEN APPROACH FOR SIMULTANEOUS HYDROTHERMAL INACTIVATION OF RICE BRAN LIPASE ENZYME ANDEXTRACTION OF ITS EDIBLE OIL USING SUBCRITICAL WATER. |
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Pourali O., Asghari F.-S. and Yoshida H., Osaka Prefecture University (Japan) |
| |
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| C04 |
CORK TREATMENT – NEW INDUSTRIAL APPLICATION OF SUPERCRITICAL FLUIDS. |
| |
Lack E., and Seidlitz H., Natex Prozesstechnologie GesmH, Ternitz (Austria), Bakali M. and Zobel R., Diamant Technoenologie S.A., San Vicente de Icantara (Spain) |
| |
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| C05 |
SUPERCRITICAL CARBON DIOXIDE EXTRACTION OF PLANT MATERIALS AT ULTRA HIGH PRESSURE. |
| |
Luetge C ., Steinhagen V., Bork M., Uhde High Pressure Technologies GmbH, Hagen (Germany) and Knez Z., University of Marior (Slovenia) |
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| C06 |
DIFFUSION RATE INCREASE DURING EXTRACTION OF POROUS PRODUCTS. THE KRISCHER APPROACH FORSUPERCRITICAL APPLICATIONS. |
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Zetzl C ., TU Hamburg-Har burg(Germany) |
