Dissertations / Theses on the topic 'Catalyst carrier'
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Couroyer, Charlotte G. M. "Attrition of alumina catalyst carrier beads." Thesis, University of Surrey, 2000. http://epubs.surrey.ac.uk/843669/.
Full textMiyazaki, Kazunari. "Studies on proton-conducting ceramic fuel cells for hydrogen-carrier utilization." Kyoto University, 2020. http://hdl.handle.net/2433/254526.
Full textFerri, Giulia. "Identification and study of relevant descriptors of the solid during the synthesis of boehmite." Electronic Thesis or Diss., université Paris-Saclay, 2021. http://www.theses.fr/2021UPASG064.
Full textAn alumina catalyst carrier must have adequate mechanical and thermal properties, and promote an appropriate mass and heat transfer. These properties depend on the carrier texture, which is the result of its manufacturing process. Our study focuses on the peptization and kneading process, which involves the dispersion of boehmite powder in an acid solution. A base is then added to induce the agglomeration of dispersed boehmite particles. This process, performed under mixing, enables to tune the size and structure of the boehmite agglomerates that will build the solid catalyst carrier. This work aims at modeling the alumina solid structure depending on the physical-chemical parameters that drive the colloidal agglomeration when no hydrodynamic forces are present. In order to study the impact of pH, ionic strength and concentration on the coagulation kinetics, three experimental techniques are used: Dynamic Light Scattering (DLS), Small Angle X-Ray Scattering (SAXS) and Scanning Transmission Electron Microscopy (STEM). The results of the experimental data are interpreted in terms of the population-balance equation, where the size-structure relationship is given by a Brownian dynamics model. The results of the population-balance model are then used as inputs for a morphological agglomeration model, to simulate large volumes of the porous structure of the real alumina solid. Such a model is one of the new contributions of this work, and enables to compute textural properties of a boehmite grain
Векшин, Віталій Олександрович. "Очищення викидних газів абсорбції від оксидів нітрогену у виробництві нітратної кислоти." Thesis, НТУ "ХПІ", 2016. http://repository.kpi.kharkov.ua/handle/KhPI-Press/22711.
Full textThesis for a Candidate of Techical Sciences degree by speciality 05.17.01 – Technology of inorganic substances. – National technical university "Kharkov polytechnical institute", Kharkov, 2016. Thesis is devoted to the development of technology for preparing the catalyst for industrial processes of selective catalytic reduction (SCR) of nitrogen oxides with ammonia. Optimal technological parameters of preparation of carrier based of titanium oxide for following impregnation with catalytically active substance have been experimentally determined. Optimal parameters of application of the active substance – platinum – from solution of hexachloroplatinic acid on the surface of carrier have been found: the number of impregnations is 1, the impregnation time is 5 min, the concentration of the impregnation solution is 10%. The positive influence of modifiers – monobasic organic acids – on the catalyst preparation by impregnation has been proved. Application of formic acid in impregnation as a competing adsorbate and as a reducing agent has been substantiated by means of physico-chemical investigations. Experimental researches of the influence of industrial parameters (temperature, gas hourly space velocity) on the activity of obtained catalysts have been carried out. Correlation between the size of platinum crystallites and the time of catalyst operation has been determined. It obeys the exponential dependence and shows decrease in running time of the catalyst with increase in size of crystallites during sintering. Mathematical model of the SCR process has been developed. Kinetic investigations of the process of NOx reduction on obtained catalysts have been carried out. They allowed to determine the optimal conditions of purification, which are as follows: the maximum degree of reduction can be achieved at T = 473 – 523 K and the bulk gas flow 50 000 – 60 000 m³/h on a catalyst modified with formic acid. The designs of the block catalyst having cellular structure and industrial reactor for it have been suggested. It is shown that the gas flow resistance of the developed catalyst is 12 times lower than that of the ABK-10. Ecological-economic calculations and economic benefit estimation show that decrease of gas flow resistance and 2.5-fold ecological costs reduction will result in savings of 16,038,720 UAH during 8 years, i.e. during full period of catalyst operation.
Векшин, Віталій Олександрович. "Очищення викидних газів абсорбції від оксидів нітрогену у виробництві нітратної кислоти." Thesis, НТУ "ХПІ", 2016. http://repository.kpi.kharkov.ua/handle/KhPI-Press/22710.
Full textThesis for a Candidate of Techical Sciences degree by speciality 05.17.01 – Technology of inorganic substances. – National technical university "Kharkov polytechnical institute", Kharkov, 2016. Thesis is devoted to the development of technology for preparing the catalyst for industrial processes of selective catalytic reduction (SCR) of nitrogen oxides with ammonia. Optimal technological parameters of preparation of carrier based of titanium oxide for following impregnation with catalytically active substance have been experimentally determined. Optimal parameters of application of the active substance – platinum – from solution of hexachloroplatinic acid on the surface of carrier have been found: the number of impregnations is 1, the impregnation time is 5 min, the concentration of the impregnation solution is 10%. The positive influence of modifiers – monobasic organic acids – on the catalyst preparation by impregnation has been proved. Application of formic acid in impregnation as a competing adsorbate and as a reducing agent has been substantiated by means of physico-chemical investigations. Experimental researches of the influence of industrial parameters (temperature, gas hourly space velocity) on the activity of obtained catalysts have been carried out. Correlation between the size of platinum crystallites and the time of catalyst operation has been determined. It obeys the exponential dependence and shows decrease in running time of the catalyst with increase in size of crystallites during sintering. Mathematical model of the SCR process has been developed. Kinetic investigations of the process of NOx reduction on obtained catalysts have been carried out. They allowed to determine the optimal conditions of purification, which are as follows: the maximum degree of reduction can be achieved at T = 473 – 523 K and the bulk gas flow 50 000 – 60 000 m³/h on a catalyst modified with formic acid. The designs of the block catalyst having cellular structure and industrial reactor for it have been suggested. It is shown that the gas flow resistance of the developed catalyst is 12 times lower than that of the ABK-10. Ecological-economic calculations and economic benefit estimation show that decrease of gas flow resistance and 2.5-fold ecological costs reduction will result in savings of 16,038,720 UAH during 8 years, i.e. during full period of catalyst operation.
Jang, Yong-Jun. "Nanosized polymer carriers for metallocene catalysts in heterogeneous olefin polymerization." [S.l.] : [s.n.], 2005. http://deposit.ddb.de/cgi-bin/dokserv?idn=976096374.
Full textLindner-Lopez, Eduard. "Heterogenised palladium catalysts and magnetic carriers for fine chemicals production." Thesis, Imperial College London, 2004. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.416028.
Full textCarriel, Schmitt Caroline [Verfasser]. "Catalytic upgrading of fast pyrolysis bio-oils applying nickel-based catalysts / Caroline Carriel Schmitt." Karlsruhe : KIT-Bibliothek, 2021. http://d-nb.info/1225401259/34.
Full textGleichweit, Christoph Verfasser], Hans-Peter [Akademischer Betreuer] Steinrück, and Jörg [Akademischer Betreuer] [Libuda. "Dehydrogenation of Liquid Organic Hydrogen Carriers on Model Catalyst Surfaces / Christoph Gleichweit. Gutachter: Hans-Peter Steinrück ; Jörg Libuda." Erlangen : Friedrich-Alexander-Universität Erlangen-Nürnberg (FAU), 2015. http://d-nb.info/1079718621/34.
Full textZhou, Shanshan. "PORE-CONFINED CARRIERS AND BIOMOLECULES IN MESOPOROUS SILICA FOR BIOMIMETIC SEPARATION AND TARGETING." UKnowledge, 2017. http://uknowledge.uky.edu/cme_etds/78.
Full textChung, Elena Yin-Yin. "Investigation of Chemical Looping Oxygen Carriers and Processes for Hydrocarbon Oxidation and Selective Alkane Oxidation to Chemicals." The Ohio State University, 2016. http://rave.ohiolink.edu/etdc/view?acc_num=osu1469182957.
Full textCarrero, Marquez Carlos Alberto [Verfasser], and Reinhard [Akademischer Betreuer] Schomäcker. "Kinetic investigation for the oxidative dehydrogenation of propane (ODP) at tailored ternary (VO x) n-(TiO x) n /SBA15 catalysts / Carlos Alberto Carrero Marquez. Betreuer: Reinhard Schomäcker." Berlin : Universitätsbibliothek der Technischen Universität Berlin, 2012. http://d-nb.info/1028912897/34.
Full textO'Connor, Timothy F. III. "Synthesis and Dynamics of Photocatalytic Type-II ZnSe/CdS/Pt Metal-Semiconductor Heteronanostructures." Bowling Green State University / OhioLINK, 2012. http://rave.ohiolink.edu/etdc/view?acc_num=bgsu1340038781.
Full textFreifrau, von Seckendorff-Gutend Jennie [Verfasser], Kai-Olaf Martin [Akademischer Betreuer] Hinrichsen, Kai-Olaf Martin [Gutachter] Hinrichsen, Dirk [Gutachter] Weuster-Botz, and Gregor D. [Gutachter] Wehinger. "Shape Matters - Experimental and Numerical Study on the Catalyst Carrier’s Geometry and the Utilization of 3d Printing herefor / Jennie Freifrau von Seckendorff-Gutend ; Gutachter: Kai-Olaf Martin Hinrichsen, Dirk Weuster-Botz, Gregor D. Wehinger ; Betreuer: Kai-Olaf Martin Hinrichsen." München : Universitätsbibliothek der TU München, 2021. http://d-nb.info/1230985190/34.
Full textMaigné, Alan. "Caractérisation et modélisation par microscopie électronique en transmission à balayage (STEM) et spectroscopie de perte d’énergie d’électrons (EELS) de « nanohorns » de carbone monofeuillet fonctionnalisés pour des applications pharmaceutiques Review of recent advances in spectrum imaging and its extension to reciprocal space Revealing the Secret of Water-Assisted Carbon Nanotube Synthesis by Microscopic Observation of the Interaction of Water on the Catalysts Role of Subsurface Diffusion and Ostwald Ripening in Catalyst Formation for Single-Walled Carbon Nanotube Forest Growth Effect of hole size on the incorporation of C60 molecules inside single-wall carbon nanohorns and their release Adsorption Phenomena of Tetracyano-p-quinodimethane on Single-Wall Carbon Nanohorns Carbon Nanohorns as Anticancer Drug Carriers Effect of Functional Groups at Hole Edges on Cisplatin Release from Inside Single-Wall Carbon Nanohorns Optimum Hole-Opening Condition for Cisplatin Incorporation in Single-Wall Carbon Nanohorns and Its Release Functionalization of Carbon Nanohorns with Azomethine Ylides: Towards Solubility Enhancement and Electron-Transfer Processes Aqueous carbon nanohorn–pyrene–porphyrin nanoensembles: Controlling charge-transfer interactions Photoinduced Electron Transfer on Aqueous Carbon Nanohorn–Pyrene– Tetrathiafulvalene Architectures Soluble Functionalized Carbon Nanohorns." Thesis, Université Paris-Saclay (ComUE), 2017. http://www.theses.fr/2017SACLS600.
Full textIn this manuscript, we will expose the characterization and modelling of Single Wall Nanohorns (SWNH) and Nanotube Forests by analytical microscopy and the functionalization of SWNH for drug delivery applications. Firstly, we will introduce the microscopy and spectroscopy methods used for our experiments. We will then study the growth process of Single Wall Carbon Nanotubes (SWCNT) forests (within the framework of a collaboration with AIST, Japan). SWCH, their structure, modifications and filling properties will be analysed in details. An original method will be presented to study the porosity of inorganic material with EELS. Ab initio calculation will also be used to explore the effect of the defects present in the SWNH wall on the oxidation and filling process. We will study the potentialities of Single Wall Carbon nanohorns as Drug Delivery Systems and particularly as anticancer drug carriers
Lin, Chuan-Zong, and 林傳宗. "Dissolution Precipitation Graphite as carrier of platinum catalyst for PEMFC." Thesis, 2006. http://ndltd.ncl.edu.tw/handle/22296817304873645823.
Full text國立臺灣大學
材料科學與工程學研究所
95
Proton exchange membrane fuel cell is a clean energy. After hydrogen oxidation and oxygen reduction, the final product is water. The catalysts and membrane play an important role in fuel cell system. The platinum and platinum- ruthenium was the most popular catalyst. And the support was usually carbon black. Carbon black had good conductivity and large specific surface area. The surface of carbon black is oxidized under the cathode environment of a PEFC. Thus, the platinum particles would be agglomerated. In this work, the DPG powders containing few CNTs(carbon nanotubes) and three dimension structure graphite were used as the support of catalyst in proton exchange membrane fuel cell. The CNTs(carbon nanotubes) and three dimension structure graphite might make the catalyst disperse well and the promotion of the electrochemical performance. TEM image of the Pt nanoparticles were obtained by using a JEM-2000FX operating at 200 kV. Exchange current was obtained by cyclic voltammetry method. Exchange current of catalyst supported on mixing powders containing 30 wt.% DPG are higher by 9% and 19%, respectively, than exchange current of catalyst supported on 100wt.% carbon black. The DPG powders containing few fullerenes and CNTs(carbon nanotubes) could be used as the support of catalyst in proton exchange membrane fuel cell.
Rao, Sudershan T. "Effect of carbon-oxygen surface complexes on the surface and catalyst carrier properties of sugar charcoal." Thesis, 1991. http://localhost:8080/iit/handle/2074/3510.
Full textWang, Wei Sheun, and 汪慰萱. "Evaluation of Zeolite L as Catalyst Carrier and Analysis of Reaction Mechanism for Dehydroisomerization of n-Butane." Thesis, 1993. http://ndltd.ncl.edu.tw/handle/14998645658123932629.
Full textShiau, Shich Chin, and 蕭旭欽. "Evaluation of γ-Al2O3 as Catalyst Carrier and Analysis of Reaction Mechanism for Dehydroisomerization of n-Butane." Thesis, 1993. http://ndltd.ncl.edu.tw/handle/71101072222454118961.
Full text東海大學
化學工程研究所
81
Isobutylene is raw material for many important petrochemicals , and it also reacts with methanol to form methyl-tertiary-butyl- ether(MTBE), which is an excellent gasoline blending material for cleaner auto exhaust. This researh study the feasibility of using γ-Al2O3 as carrier impregnated with metal to form bi- functional catalyst for dehydroisomerization of n-butane. Experimental data showed that reaction temperature around 823K offered best results. Reaction with (0.05% Pt + 0.5% Ga)/γ-Al2 O3 catalyst at 823K and space time of 0.3 s yielded 14% conversion of n-butane, and 70% and 16% selectivies of total butenes and isobutylene, respectively. This reaction system could be lumped as a network of three reactions, namely dehydrogenation, isomerization, and side reaction. Dehydrogenation reation had an intrinsic activation energy of 25 kJ/mol;Skeletal isomerization reaction had an intrinsic activation energyof 44 kJ/mol; Side reaction had an intrinsic activation energy of 135 kJ/mol.
Lu, Po-Chang, and 盧柏璋. "Application of Taguchi Method in the Optimization of the Porous Ceramic Catalyst Carrier Fabricated by Replica Method." Thesis, 2018. http://ndltd.ncl.edu.tw/handle/bef3q4.
Full text國立臺北科技大學
資源工程研究所
106
Ammonia is a toxic substance commonly used in industry. If it is directly discharged into the atmosphere without being treated or directly inhaled by the human body, it will cause significant damage to the environment and human body. Reducing the concentration of ammonia emissions is often achieved through the "oxidation catalytic method." The composition of the catalyst can be divided into two parts: catalyst material and carrier. This study focuses on the synthesis of the catalyst carrier. Taguchi experimental design method was used to synthesis porous ceramics as a catalyst carrier material by replica method, and the effects of parameters such as ratio of ceramic slurry, sintering temperature, and sintering time on the compressive strength and porosity of the support material were investigated. In this study, kaolin and other additives were used to make the ceramic slurry, and the PU template was impregnated to coat the slurry on the template. The template was burned and sintered to form a carrier material after high temperature. Taguchi analysis showed that a PVA(aq) with a molecular weight of 77,500 was selected as a solvent to prepare a 50 wt.% kaolin solution, and 3 wt.% albite powder was additionally added as a flux. After the excess slurry was removed by extrusion-type de-slurry, sintering was performed. After holding temperature at 1150°C for 7 hours to form the sample, the secondary slurry penetrates into the sample through negative pressure to perform sintering. The best compressive strength can be obtained initially, reaching 1.74 MPa. Using a PVA with a molecular weight of 121000 as a solvent, 33 wt.% kaolin slurry was prepared, and 3 wt.% of glass powder was additionally added as a fluxing agent. After the excess slurry was removed by blowing, sintering was performed at 1100°C for 9 hours to obtain the best porosity, which is 93.07% Compared with commercially available honeycomb supports, although the compressive strength is not as good as commercially available honeycomb supports, their porosity is much higher than that of commercially available supports, and their mass is also much lighter than that of commercially available monomers. Catalytic properties are also inferior to commercial ones. The compressive strength of reticulated porous ceramics synthesized by the optimum level parameters in this study was 3.17 MPa, and the porosity was 52.38%. All of L18s used compounding ratios were able to successfully synthesize reticulated porous ceramic materials with basic mechanical properties. Compared with commercially available honeycomb supports, although their compressive strength is not as good as commercially available honeycomb supports, their porosity is higher than that of commercially available supports, their mass is also much lighter than that of commercially available supports. The catalytic activity of Ammonia gas conversion efficiency is also not inferior to the commercial support.
Korzeniowska, Aleksandra. "Nanostrukturalne materiały porowate jako katalizatory oraz nośniki leków w medycynie i ochronie środowiska." Praca doktorska, 2019. https://ruj.uj.edu.pl/xmlui/handle/item/77303.
Full textCHEN, JIA-YIN, and 陳佳吟. "Application and synthesis of pyridine crown ether analogs phase transfer catalyst and magnesium ion transport crown ether carrier in liquid membrane." Thesis, 1992. http://ndltd.ncl.edu.tw/handle/01722969741202099422.
Full textHansen, Steven Paul. "Ion selectivity in carrier-mediated dialysis and electrodialysis." Thesis, 2012. http://hdl.handle.net/1828/3975.
Full textGraduate
Li, Yun-Ling, and 李芸菱. "The photocalytical removal of trichloroethylene in water by clay-carrier impregnated with metal catalysts." Thesis, 2006. http://ndltd.ncl.edu.tw/handle/43357022155063493774.
Full text國立屏東科技大學
環境工程與科學系
94
The chloride organic compounds have potential carcinogenic, tumor, and monster characteristics. Among these carcinogenic substances, trichloroethylene (TCE) is an artificial synthesis material. When it exposes to the atmosphere, it will influence the environment and health. In view of this, in this study, modifications of clay minerals are conducted to form clay catalysts and are illuminated with visible light in order to carry on photocatalysis to degrade the TCE. The main purpose is to discuss the possible mechanism and impact when clay catalysts are performing photocatalytical degradation with visible light. The main clay carriers include smectite clay and guan-shan series soil and the catalysts are sm-Ti, sm-Ag, sm-Zn, Ks-Ti, Ks-Ag, and Ks-Zn to perform the batch and fixed continuous experiment and find out the photocatalytic efficiency and mineralization with different catalysts. The study shows that the adding amount of 0.08 wt% and 0.1 wt% have the best degradation efficiency on TCE. When more quantity of catalysts is added, the easier it is for the shielding effect to take place. This is because the catalyst carrier possesses better adsorbability on TCE so that the total degradation rate on TCE involves the adsorption rate and net degradation rate. In the batch and fixed continuous experiment, the suspension catalysts can achieve the fine degradation and adsorption efficiency; while the total and net degradation rate of fixed continuous experiment decrease with the increase of the rate of utilization. It presumes that the decrease of the active sites and surface area of catalysts and the production of the kinds of ions and the change of pH about cement boards. Therefore, the degradation efficiency of suspension catalysts is better than that of fixed continuous experiment on TCE. In mineralization, the total and net mineralization rate is in decreasing trend with the catalysis time. It is assumed that during the degradation, intermediates are produced causing the reduce of energy and slow down of mineralization rate. In the identification of intermediates, the above-mentioned methods can be shown that the intermediates can be produced and the concentration has trend of increase with the experiment time and the times of experiment. The intermediates can reduce the degradation efficiency and mineralization of catalysts on TCE.
Krasnokutskiy, E. V., B. B. Makhanov, V. E. Ved, M. I. Satayev, A. V. Ponomarenko, and A. A. Saipov. "Universal multi-functional secondary catalyst carriers for purification of gas emission of thermal power equipments." Thesis, 2016. http://repository.kpi.kharkov.ua/handle/KhPI-Press/28164.
Full textBhat, Imtiyaz Ahmad. "Design and Application of Self-Assembled Coordination Cages for Catalysis and as Drug Carrier." Thesis, 2018. https://etd.iisc.ac.in/handle/2005/5350.
Full text劉翼綵. "Investigation on fuel properties of biodiesel produced through transesterification using heterogeneous catalyst carried by coal fly ash." Thesis, 2012. http://ndltd.ncl.edu.tw/handle/25878060205345664348.
Full textJang, Yong-Jun [Verfasser]. "Nanosized polymer carriers for metallocene catalysts in heterogeneous olefin polymerization / vorgelegt von Yong-Jun Jang." 2005. http://d-nb.info/976096374/34.
Full textHsieh, Cheng-Yu, and 謝正裕. "Synthesis and Application of Larient-type Crown Ethers as Ion Transport Carriers and Phase Transfer Catalysts." Thesis, 1993. http://ndltd.ncl.edu.tw/handle/38809071851401176556.
Full text國立師範大學
化學學系
81
The carboxylate crown ethers (sym-hydroxydibenzo-16- crown-5, DB16C5OH and sym-dibenzo-16-crown-5-oxyacetic acid, DB16C5COOH) were synthesized to apply as ion transport carriers and play as phase transfer catalyst (PTC) in organic synthesis. In the study of Na+ ion transport with sym-DB16C5COOH ,it seems to indicate that the bigger counter anion and more hydrophobic anions of sodium salts exhibited better transport.Besides the solvation of the salts, the pH values of source solution and target solution showed some effect on Na+ ion transport. In addition ,crown ethers effect on the Na+ ion transport was investigated ,the Na+ ion transport ability of various crown ethers seems to decrease in the order : DB16C5COOH>B15C5COOH> DB16C5OH>B15C5,it shows that side chain functional group on crown ethers may influence the Na+ ion transport ability. Crown ethers were applied as phase transfer catalyst (PTC) in the Claisen condensation reaction between ethyl acetate and ethyl benzoate.It showed that DB16C5OH was quite a good catalyst in the reaction which can increase the yield of the product from 10% to 70% for only 6 hours. The effects of crown ethers on the yield of the product were in the order: DB16C5OH > B15C5 > DB18 C6 >Blank>DB16C5COOH. Effect of solvent and temperature on the catalytic Claisen condensation reaction were also investigated. The reaction in lower polar solvents seems to show higher yield . The temperature study on the catalytic reaction reveals that it has a optimum temperature at 40oC and with the order 40oC > 60oC > 25oC . This maybe attributed to high solubility of NaOEt, but less stability of Na+/crown ether complexes at higher temperature . Concentration effect of crown ethers and reactant were also studied and discussed. The best result was obtained with the ratio crown ether/ reactants = 1/1.
Hsu, Li-Yeh, and 徐禮業. "Studies on Catalytic Reduction of NO with NH3 over Cu Catalysts Supported on Carbon and Other Carriers." Thesis, 2003. http://ndltd.ncl.edu.tw/handle/34599992327805779636.
Full text國立成功大學
化學工程學系碩博士班
91
The most widely employed catalysts in the SCR process are made of metal oxides or zeolites, which have optimum reaction temperatures ranging within 270–430 °C. Under this circumstance, reheating would be needed to bring the flue gas to the desired temperature if the catalyst bed were to be situated after the electrostatic precipitator and desulurization plant. The operative coats of SCR using the present catalysts are very expensive. In this study, we went to develop the more chip, lower operation temperature, and high activity of catalysts to replace the present catalysts. We found that the redox properties of copper oxide could be changed by the nature of supports and influence the activity of catalysts. The copper oxide over activated carbon is easily reduced and there is a good catalytic activity for NO reduction below 250 ºC. In addition, there are no activity over activated carbon (PFC) without ash content for catalytic NO reduction with NH3. The CuO impregnated on PFC can clearly increase activity of catalysts. The activity increases with the impregnated amount of CuO. The existences of oxygen-containing functional groups and copper oxide over activated carbon will increase the activity for NO reduction with NH3. Compared with CuO over PFC, oxygen-containing functional groups has less activity. The activity of catalysts is influenced by the dispersion of copper oxide over PFC. However, the disactivated catalysts, made by the higher heat treatment, can be regenerated by 1N HNO3. For selective catalytic NO reduction with NH3, NO conversion is near 100% over PFC catalyst, impregnated 8 wt.% CuO, at 200 ºC. In the kinetic studies, Mars-van Krevelen model can fit the data of copper-supported catalysts. And the behavior of catalysts can be predicted at different reaction conditions by Mars-van Krevelen model.
Ronovský, Michal. "Vysoce uspořádané tenké vrstvy oxidu kobaltu pro modelovou katalýzu." Master's thesis, 2020. http://www.nusl.cz/ntk/nusl-415468.
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