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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3.semester(MS)<br />
Laboratory<br />
M.Polakovič<br />
Safety Engineering I 2/1/0 L.Jelemenský, Z.Švandová<br />
Explosion Prevention<br />
Lectures<br />
Laboratory<br />
2/0/2<br />
L.Jelemenský<br />
J.Labovský<br />
Electrical Safety for Chemical<br />
Process Plants<br />
Biochemical Engineering<br />
1/0/1 D.Perniš<br />
2/0/1 Polakovič<br />
Lectures<br />
Safety Engineering 2/0/0 Jelemenský<br />
Advanced Laboratory of Chemical 0/0/6 E.Graczová, L.Jelemenský,<br />
Engineering IV<br />
M.Juma, M.Polakovič, J.Stopka,<br />
J.Šefčík Š.Schlosser, P.Steltenpohl<br />
, P.Timár<br />
Process System Engineering 1/0/2<br />
Lectures<br />
Laboratory<br />
J.Markoš,<br />
M.Juma<br />
Chemical Reaction Engineering II 2/0/1 J.Markoš<br />
Cost Engineering of Industrials 0/2/0 M.Bafrnec<br />
Energetic Design Project 0/0/2 O.Mierka<br />
Solid Particles in Technology and 2/0/0 P.Timár<br />
Environment<br />
Bioprocess Engineering II<br />
Lectures<br />
1/0/1<br />
V.Báleš<br />
Laboratory<br />
3.semester(MS) Process System Engineering 2/0/2<br />
Lectures<br />
Laboratory<br />
J.Markoš<br />
M.Juma<br />
Advanced Laboratory of Chemical<br />
Engineering I<br />
0/0/4 M.Juma, L.Jlemenský<br />
O.Mierka, , P.Steltenpohl, J.Stopka,<br />
Safety Engineering II 2/1/0 L.Jelemenský, Z.Švandová<br />
Laboratory of Process Plant Safety 0/0/3<br />
L.Jelemenský<br />
Reaction Engineering II 2/0/0 J.Markoš<br />
4. semester (MS) Master Thésis 0/0/27 E. Graczová, M.Juraščík, J.Markoš,<br />
O.Mierka, P.Steltenpohl,<br />
M.Polakovič, J.Stopka,<br />
IV. CURRENT RESEARCH PROJECTS<br />
APVT-20-000804 Modeling, simulation and safety analysis of reactive distillation units in<br />
chemical industry (Jozef Markoš)<br />
The design of a reactive distillation unit requires detailed knowledge of the reaction kinetics and equilibria of all<br />
reactions, vapour - liquid equilibria, and, in the case of heterogeneous catalysis, knowledge of transport<br />
phenomena in the catalyst particle as well. Through a mathematical model describing the unit properly, it is<br />
possible to predict changes of the performance parameters switching the unit from one steady state to another<br />
one, to find out how to avoid such situation, and how to set the initial parameters for start-up of the unit in order to<br />
reach the desired steady state, etc. The aim of the proposed project is to develop such model, to test it using real<br />
data from the literature, and to use it for safety analysis, mainly for multiple steady state identification, parametric<br />
sensitivity and response of the system to changes of the performance parameters.<br />
Project duration: from 01.01.2005 to 31.12.2007<br />
VEGA 1/1377/04 Quantitative framework for safety analysis of chemical reactors (Ľudovít<br />
Jelemenský)<br />
The effectiveness of any method used to identify hazards in chemical processes such as chemical reactors<br />
affects both safety and economics. To achieve maximum safety at minimum cost, a conservative but realistic<br />
hazard analysis must be carried out. The aim of the project is to further develop the integrated hazard simulation<br />
program, which was developed by our research group during the previous project. The extension of the integrated<br />
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