"gas purification; adsorption; catalytic oxidation; VOC"@en . . . "[E7DF10EEA980]" . "Metodika n\u00E1vrhu adsorp\u010Dn\u011B - oxida\u010Dn\u011B katalytick\u00E9ho za\u0159\u00EDzen\u00ED pro likvidaci VOC z odpadn\u00EDho vzduchu"@cs . "Filtra\u010Dn\u00ED technika, spol. s r. o." . . "325850" . "2009-10-31+01:00"^^ . "Design procedure for adsorption - catalytic oxidation equipment for VOC liquidation from waste air"@en . . "U12118" . "P(FR-TI1/173)" . "2"^^ . . . "Soubor znalost\u00ED a v\u00FDpo\u010Dtov\u00E9 programy - MATLAB, v\u010Detn\u011B nastaviteln\u00FDch konstant - know how." . "2"^^ . "\u0160r\u00E1mek, Michal" . . "Soubor znalost\u00ED a v\u00FDpo\u010Dtov\u00E9 programy - MATLAB, v\u010Detn\u011B nastaviteln\u00FDch konstant - know how." . "Metodika n\u00E1vrhu adsorp\u010Dn\u011B - oxida\u010Dn\u011B katalytick\u00E9ho za\u0159\u00EDzen\u00ED pro likvidaci VOC z odpadn\u00EDho vzduchu"@cs . "RIV/68407700:21220/09:00164211" . "21220" . . "12118-MET-2009-01" . . . . . "Large volumes of gas polluted by low concentrations of volatile organic compounds (VOCs) are usually cleaned by adsorption. Adsorption columns are regenerated by hot air. VOCs released into desorption cycle are decomposed by oxidation catalysis. These operations have to be coordinated so that the oxidation runs auto-thermally. This methodology is focused on a modeling of the system briefly described above with the aim to propose a model enabling design and optimization of the equipment. The general model consists of particular models for adsorption, catalytic oxidation, and desorption including a discrete regulation. MATLAB tools are used effectively for the numerical solution of the proposed mathematical models. When using proposed mathematical models one can avoid difficulties arising from changing the process condition and the scale-up. Such a system reduces operational costs remarkably, as compared to a direct VOC removal using oxidation processes."@en . "RIV/68407700:21220/09:00164211!RIV12-MPO-21220___" . "\u010Ci\u0161t\u011Bn\u00ED velk\u00FDch objem\u016F vzduchu s n\u00EDzk\u00FDm obsahem t\u011Bkav\u00FDch organick\u00FDch l\u00E1tek (VOC) se prov\u00E1d\u00ED v adsorp\u010Dn\u00EDch apar\u00E1tech. Regenerace t\u011Bchto apar\u00E1t\u016F se prov\u00E1d\u00ED hork\u00FDm vzduchem. VOC desorbovan\u00E9 hork\u00FDm vzduchem se pak likviduj\u00ED pomoc\u00ED oxida\u010Dn\u00EDch proces\u016F. Tyto operace mus\u00ED b\u00FDt slad\u011Bny tak, aby oxidace prob\u00EDhala v autotermn\u00EDm re\u017Eimu. Tato pr\u00E1ce se zab\u00FDv\u00E1 modelov\u00E1n\u00EDm uveden\u00E9ho syst\u00E9mu s c\u00EDlem vytvo\u0159it model umo\u017E\u0148uj\u00EDc\u00ED n\u00E1vrh a optimalizaci za\u0159\u00EDzen\u00ED. Celkov\u00FD model se skl\u00E1d\u00E1 z blok\u016F pro adsorpci, katalytickou oxidaci a desorpci \u0159\u00EDzenou diskr\u00E9tn\u00EDm regul\u00E1torem. Pro numerick\u00E9 \u0159e\u0161en\u00ED model\u016F je efektivn\u011B vyu\u017Eito jednotliv\u00FDch n\u00E1stroj\u016F MATLABU. Vyu\u017Eit\u00EDm navr\u017Een\u00FDch model\u016F lze p\u0159edej\u00EDt nejistot\u00E1m p\u0159i zm\u011Bn\u011B provozn\u00EDch podm\u00EDnek a p\u0159i p\u0159echodu od poloprovozn\u00EDho za\u0159\u00EDzen\u00ED k pr\u016Fmyslov\u00E9mu. Tento zp\u016Fsob \u010Di\u0161t\u011Bn\u00ED vzduchu v\u00FDrazn\u011B sni\u017Euje provozn\u00ED n\u00E1klady oproti p\u0159\u00EDm\u00FDm metod\u00E1m likvidace VOC pomoc\u00ED oxida\u010Dn\u00EDch proces\u016F."@cs . "Ditl, Pavel" . "Design procedure for adsorption - catalytic oxidation equipment for VOC liquidation from waste air"@en . . . . "\u010Ci\u0161t\u011Bn\u00ED velk\u00FDch objem\u016F vzduchu s n\u00EDzk\u00FDm obsahem t\u011Bkav\u00FDch organick\u00FDch l\u00E1tek (VOC) se prov\u00E1d\u00ED v adsorp\u010Dn\u00EDch apar\u00E1tech. Regenerace t\u011Bchto apar\u00E1t\u016F se prov\u00E1d\u00ED hork\u00FDm vzduchem. VOC desorbovan\u00E9 hork\u00FDm vzduchem se pak likviduj\u00ED pomoc\u00ED oxida\u010Dn\u00EDch proces\u016F. Tyto operace mus\u00ED b\u00FDt slad\u011Bny tak, aby oxidace prob\u00EDhala v autotermn\u00EDm re\u017Eimu. Tato pr\u00E1ce se zab\u00FDv\u00E1 modelov\u00E1n\u00EDm uveden\u00E9ho syst\u00E9mu s c\u00EDlem vytvo\u0159it model umo\u017E\u0148uj\u00EDc\u00ED n\u00E1vrh a optimalizaci za\u0159\u00EDzen\u00ED. Celkov\u00FD model se skl\u00E1d\u00E1 z blok\u016F pro adsorpci, katalytickou oxidaci a desorpci \u0159\u00EDzenou diskr\u00E9tn\u00EDm regul\u00E1torem. Pro numerick\u00E9 \u0159e\u0161en\u00ED model\u016F je efektivn\u011B vyu\u017Eito jednotliv\u00FDch n\u00E1stroj\u016F MATLABU. Vyu\u017Eit\u00EDm navr\u017Een\u00FDch model\u016F lze p\u0159edej\u00EDt nejistot\u00E1m p\u0159i zm\u011Bn\u011B provozn\u00EDch podm\u00EDnek a p\u0159i p\u0159echodu od poloprovozn\u00EDho za\u0159\u00EDzen\u00ED k pr\u016Fmyslov\u00E9mu. Tento zp\u016Fsob \u010Di\u0161t\u011Bn\u00ED vzduchu v\u00FDrazn\u011B sni\u017Euje provozn\u00ED n\u00E1klady oproti p\u0159\u00EDm\u00FDm metod\u00E1m likvidace VOC pomoc\u00ED oxida\u010Dn\u00EDch proces\u016F." . . . "\u00FAspora \u010Dasu regenerace 40%" . "Metodika n\u00E1vrhu adsorp\u010Dn\u011B - oxida\u010Dn\u011B katalytick\u00E9ho za\u0159\u00EDzen\u00ED pro likvidaci VOC z odpadn\u00EDho vzduchu" . "Metodika n\u00E1vrhu adsorp\u010Dn\u011B - oxida\u010Dn\u011B katalytick\u00E9ho za\u0159\u00EDzen\u00ED pro likvidaci VOC z odpadn\u00EDho vzduchu" .