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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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