National Repository of Grey Literature 36 records found  1 - 10nextend  jump to record: Search took 0.01 seconds. 
Phenol Removal from Contaminated Water by Various Active Carbons
Matějková, Martina ; Papežová, Barbora ; Šolcová, Olga
This study is focused on evaluation of the individual sorbent efficiency and capacity for phenol removal from contaminated water.
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Plný tet: SKMBT_C22014090110380 - Download fulltextPDF
Titanium Dioxide as Photocatalytic Agent
Spáčilová, Lucie ; Maléterová, Ywetta ; Křesinová, Zdena ; Cajthaml, Tomáš ; Šolcová, Olga
Based on the laboratory results the arrangement of experiments with the real wastewater from the municipal sewage treatment plants was chosen.
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Plný tet: SKMBT_C22014090110371 - Download fulltextPDF
Possible Removal of Mercury in Dry Flue Gas Cleaning Lines of Solid Waste Incineration Units
Svoboda, Karel ; Hartman, Miloslav ; Šyc, Michal ; Pohořelý, Michael ; Jeremiáš, Michal ; Kameníková, Petra ; Durda, Tomáš
Here we will focus on dry flue gas cleaning methods applied for MSW incineration. Majority of dust from the incineration is usually removed in electrostatic filters or fabric (bag) filters. Dry method of flue gas cleaning are advantageous particularly in smaller solid waste incineration units, they have usually lower capital costs and simpler operation. The dry gas cleaning methods are based on an alkali sorbent injection and fabric filters for removal of dust and solid products from cleaning (gas-solid reactions).
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Plný tet: SKMBT_C22014082908314 - Download fulltextPDF
Thermodynamic Interferences of HCl and HF in Producer Gas Desulfurization by Ce, La, Mn and Zn Based Solid Sorbents
Hartman, Miloslav ; Svoboda, Karel ; Pohořelý, Michael ; Šyc, Michal ; Jeremiáš, Michal ; Huang, Ch.-Y.
In our thermodynamic theoretical study we concentrated our attention on thermodynamics of gas-solid desulfurization reactions (H2S, COS, thiophene), properties of sorbents (melting point evaporation), attainable equilibrium sulfur compounds concentrations in gas at temperature 500 – 1100 K (227-827 oC) under conditions typical for producer gas composition. Similarly removal of HCl and HF by Ce, La, Zn, Mn and Ni oxides based sorbents is described and possible interferences in simultaneous sorption of HCl or HF with H2S are analyzed. Suitable conditions and sorbents are suggested for deep removal of sulfur compounds in presence of HCl. Conditions for efficient preliminary removal of HCl and HF by alkali-based sorbents (NaHCO3, K2CO3, Ca(OH)2, CaCO3) are suggested and possible interferences caused by H2S are analyzed in terms of attainable equilibrium concentrations of HCl and HF in presence of H2S. Properties of La and Ce-based sorbents for sulfur compounds are compared with Zn, Mn and Ni based sorbents in terms of efficiency and interferences caused by presence of hydrogen-halides (HCl, HF).
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Plný tet: SKMBT_C22014082908320 - Download fulltextPDF
Multiple Sulfidation/Regeneration Cycle Tests for Advanced Fuel Conversion Process by 20 wt%Fe2O3/Al2O3 Sorbent
Huang, C.Y. ; Chyou, Y.P. ; Svoboda, Karel
In this study, 20 wt%Fe2O3/Al2O3 was used as a sorbent to perform multiple sulfidation/regeneration cycle tests in a fixed-bed reactor under simulated hot syngas conditions. The physical properties of sorbents were analyzed by X-ray diffraction (XRD), inductively coupled plasma atomic emission spectrometry (ICP-AES), BET, and SEM/EDS. ICP-AES results indicated that the composition of metal oxide was close to the theoretical value. Multiple sulfidation/regeneration cycle tests showed that the 20wt%Fe2O3/Al2O3 can be regenerated and thus reused after the oxidation process. Due to the sulfidation reaction, colour change of the 20 wt%Fe2O3/Al2O3 sorbent was observed, from the original red to black. After six sulfidation-regeneration cycles, the sulfur capacity of the sixth cycle remained approximately on a level of 68% of the sulfur capacity in the first cycle. The BET analysis showed that the surface area decreased as the cycle number increased. The sulfidation-regeneration cycles were coupled with endothermic-exothermic reactions, which probably caused sintering of the sorbent, decreasing its surface area and sulfur capacity.
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Plný tet: SKMBT_C22014082908321 - Download fulltextPDF
Simulation of Carbonaceous Waste Partial Oxidation versus Pilot Plant Data
Tukač, V. ; Hanika, Jiří ; Veselý, Václav ; Lederer, J. ; Poslední, W. ; Nečesaný, F. ; Nečesaný, F., jr.
The goal of this work was to develop numerical model of experimental POX pilot plant reactor of UNIPETROL RPA to test application of different raw materials. Process performance was compared with results of its simulation by Aspen Plus software. Both chemical equilibrium and kinetic of pyrolysis and soot formation were taking into account. Also sensitivity of POX product composition depending on properties of different raw materials and reaction condition were analysed by mathematical modelling approach.
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Plný tet: SKMBT_C22014090110410 - Download fulltextPDF
Alcohol Ethoxylate Sulfation in a Microreactor Operated in a Pilot Plant Environment
Stavárek, Petr ; Křišťál, Jiří ; Jiřičný, Vladimír ; Vanhoutte, D. ; Tarchini, R.
The main objective of this paper is to focus on the development of a new intensified reactor for sulfation and/or sulfonation reaction which reduces change-over times and can use much higher SO3 concentrations, thus reducing capital in pre- and post-treatment of the air.
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Plný tet: SKMBT_C22014090110394 - Download fulltextPDF
Kinetics and Rate Law Determination of 2-Methylpropene Hydrogenation in a Packed-Bed Microreactor
Vajglová, Zuzana ; Stavárek, Petr ; Křišťál, Jiří ; Kolena, J. ; Jiřičný, Vladimír
This study focuses on hydrogenation of C4 fraction, more specifically on development of the methodology of kinetic data collection and evaluation. The hydrogenation of 2- methylpropene on platinum catalyst was investigated as a model reaction.
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Plný tet: SKMBT_C22014090110396 - Download fulltextPDF
Frontiers of Processing: Faster, Leaner and Targeted
Simoncelli, A. ; Křišťál, Jiří
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Plný tet: SKMBT_C22014090110386 - Download fulltextPDF

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