rok 2006 - Fakulta chemickej a potravinárskej technológie ...
rok 2006 - Fakulta chemickej a potravinárskej technológie ...
rok 2006 - Fakulta chemickej a potravinárskej technológie ...
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L. VEGA Project No 1/3581/06, Specification of prediction of multi-component vapor-liquid and<br />
liquid-liquid equilibria for the purpose of separation of liquids by distillation, extraction and<br />
extractive distillation (Elena Graczová)<br />
Specification of prediction of two-phase multi-component vapor-liquid and liquid-liquid equilibria necessary for the<br />
design of industrial separation equipment like distillation and extraction columns, and for the estimation of<br />
optimum operation conditions. Extension of the method of correlation of three-component equilibrium data of twophase<br />
systems (vapor-liquid and liquid-liquid) by the universal ternary contribution. Investigation of the influence<br />
of the ternary correction evaluated from ternary vapor-liquid equilibrium data and combined vapor-liquid and<br />
liquid-liquid data for obtaining more precise prediction of a complex two-phase four-component equilibrium.<br />
Application of the calculation for systems related to the separation of BTX aromatics with mixed extraction<br />
solvents.<br />
Project duration: from 01.<strong>2006</strong> to 12. 2008<br />
M. LPP-0181-06 Modelling of reactive separation processes (Jozef Markoš)<br />
Modelling of reactive separation processes. Industrial processes involving chemical reaction and separation in<br />
one unit are called reactive separations. Mathematical modelling of reactive separation units represents a useful<br />
tool for their design, optimization, parametric sensitivity and safety analysis. The main aim of the proposed project<br />
is to develop a non-equilibrium model of a reactive separation unit with very fast reactions in steady state and in<br />
dynamic regime and to apply the developed model for simulation of such units.<br />
Project duration: from <strong>2006</strong> to 2009<br />
N. VEGA-1/3573/06 Modelling, hydrodynamic and oxygen mass transfer in airlift bioreactors<br />
(Jozef Markoš)<br />
Modelling, hydrodynamic and oxygen mass transfer in airlift bioreactors. The use of airlift reactors in<br />
biotechnology becomes more and more extensive. In spite of this fact, most papers published in the literature<br />
deals with the use of ALRs only with model media like air – water. The aim of this project is to study the<br />
hydrodynamics and mass transfer of oxygen in real fermentation air lift bioreactors. With help of a mathematical<br />
model of the reactor and experiments in laboratory ALRs with working volumes of 10, 40 and 200 liters, the<br />
influence of a real fermentation broth on ALR hydrodynamics and scale up will be studied.<br />
Project duration: from <strong>2006</strong> to 2008<br />
O. APVV-99-004405 Study of 2-phenylethanol formation in an integrated system with<br />
continuous product separation (Vladimír Báleš)<br />
The basic aim of the project is the achievement of knowledge on biochemistry of 2-phenylethanol formation by<br />
yeasts cultivated in media with organic phase. Study of the toxic influence of the product on microbial culture and<br />
its elimination by in-situ separation in an external unit will be done. The metabolic activities of selected yeast<br />
strains (Saccharomyces sp., Kluyveromyces sp.) related to the 2-phenylethanol production will be studied.<br />
Cultivation media composition as well as the process parameters will be optimized. To minimize the toxic effects<br />
of the product towards the culture, the mechanism and characteristics of in-situ product extraction during the<br />
fermentation process will be used and studied. A suitable organic phase will be selected and tested for in-situ<br />
extraction of the product. A continuous product separation system will be constructed and integrated into the<br />
system bioreactor - in-situ extraction - separation. Finally. the integrated process for 2-phenylethanol will be<br />
designed and optimized in lab- and pilot-scale experiments. Optimal parameters of the batch and continuous<br />
processes will be proposed and described. Process data should be used for design of the industrial scale process<br />
for production of 2-phenylethanol.<br />
Project duration: from 01. 03.06 to 31.12. 09<br />
P. APVV-51-033205, Genetically modified microorganisms as whole cells biocatalysts of<br />
enantioselective biooxydations for new immobilized biotechnologies (Vladimír Štefuca)<br />
The project is aimed at the development of immobilized cell biocatalysts for oxidation of prochiral compounds<br />
through the Baeyer-Villiger reaction mechanism. The basic tasks of the Faculty involved are: 1. Development of<br />
an optimum biocatalyst particle using experimental and mathematical modeling involving kinetic and mass<br />
transfer phenomena; 2. Design and scale up of bioreactors for oxidative biotransformations of chosen<br />
compounds.<br />
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