Tesi sul tema "Catalysts – Analysis"
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Beskari, Mohamed Ali. "Dynamic analysis of diffusion and convection in porous catalysts". Thesis, University of Salford, 1997. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.244857.
Testo completoKwon, Doo Hyun. "Computational Design and Analysis of Molecular Ethylene Oligomerization Catalysts". BYU ScholarsArchive, 2019. https://scholarsarchive.byu.edu/etd/8551.
Testo completoAhuja, Vishal. "Analysis of novel transition metals as catalysts for oxygen delignification". Thesis, National Library of Canada = Bibliothèque nationale du Canada, 2001. http://www.collectionscanada.ca/obj/s4/f2/dsk3/ftp05/MQ62909.pdf.
Testo completoFomes, Charles William. "Development of novel oxidation catalysts for carbon isotope ratio analysis". Thesis, Open University, 2000. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.343742.
Testo completoLentz, Samuel D. "Development and optimization of NOx reduction catalysts using statistical analysis". Connect to resource, 2009. http://hdl.handle.net/1811/36953.
Testo completoAllcock, Gillian C. "The statistical aspects of the analysis and design of enzyme kinetic studies". Thesis, University of Newcastle Upon Tyne, 2001. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.366536.
Testo completoDai, Shuanghua Patrick. "X-ray scattering and thermal analysis study of isotactic polypropylene /". Thesis, Connect to Dissertations & Theses @ Tufts University, 2000.
Cerca il testo completoSubmitted to the Dept. of Physics. Adviser: Peggy Cebe. Includes bibliographical references (leaves 246-251). Access restricted to members of the Tufts University community. Also available via the World Wide Web;
Mullet, Dianna Rose. "Catalysts of Women's Success in Academic STEM: A Feminist Poststructural Analysis". Thesis, University of North Texas, 2017. https://digital.library.unt.edu/ark:/67531/metadc1062911/.
Testo completoHaibo, E. "Quantitative analysis of core-shell nanoparticle catalysts by scanning transmission electron microscopy". Thesis, University of Oxford, 2013. http://ora.ox.ac.uk/objects/uuid:19c3b989-0ffb-487f-8cb3-f6e9dea83e63.
Testo completoNguyen, Tuan Huy Chemical Sciences & Engineering Faculty of Engineering UNSW. "Semiconductor oxide supported Mo and Mo-W carbide catalysts for Fischer-Tropsch synthesis". Awarded by:University of New South Wales. School of Chemical Sciences and Engineering, 2006. http://handle.unsw.edu.au/1959.4/26969.
Testo completoTau, Prudence Lerato. "Study of titanium, tantalum and chromium catalysts for use in industrial transformations". Thesis, Rhodes University, 2007. http://hdl.handle.net/10962/d1005028.
Testo completoMorgan, David Rees. "In situ ¹³C NMR monitoring of the dehydration of 2-propanol over H-ZSM-5". Thesis, Virginia Polytechnic Institute and State University, 1989. http://hdl.handle.net/10919/52091.
Testo completoMaster of Science
Liu, Wei. "Preparation, characterization, and catalytic properties of alkaline earth oxide MO (M=Ca, Mg, Sr, Ba)--modified VOx/SBA-15 catalysts for the oxidative dehydrogenation of n-butane". HKBU Institutional Repository, 2007. http://repository.hkbu.edu.hk/etd_ra/885.
Testo completoNylén, Ulf. "Development of ring-opening catalysts for diesel quality improvement". Licentiate thesis, KTH, Chemical Engineering and Technology, 2004. http://urn.kb.se/resolve?urn=urn:nbn:se:kth:diva-1712.
Testo completoThe global oil refining industry with its present shift inproduct distribution towards fuels such as gasoline and dieselwill most likely hold the fort for many years to come. However,times will change and survival will very much depend onprocessing flexibility and being at the frontiers of refiningtechnology, a technology where catalysts play leading roles.Today oil refiners are faced with the challenge to producefuels that meet increasingly tight environmentalspecifications, in particular with respect to maximum sulphurcontent. At the same time, the quality of crude oil is becomingworse with higher amounts of polyaromatics, heteroatoms(sulphur and nitrogen) and heavy metals. In order to staycompetitive, it is desirable to upgrade dense streams withinthe refinery to value-added products. For example, upgradingthe fluid catalytic cracking (FCC) by-product light cycle oil(LCO) into a high quality diesel blending component is a veryattractive route and might involve a two-step catalyticprocess. In the first step the LCO is hydrotreated andheteroatoms are removed and polyaromatics are saturated, in thesecond step naphthenic rings are selectively opened to improvethe cetane number of the final product.
The present research is devoted to the second catalytic stepof LCO upgrading and was carried out within the framework of aEuropean Union project entitled RESCATS.
From the patent literature it is evident that iridium-basedcatalysts seem to be good candidates for ring-opening purposes.A literature survey covering ring opening of naphthenicmolecules shows the need for extending investigations toheavier model substances, more representative of the dieselfraction than model compounds such as alkylated mono C5 and C6-naphthenic rings frequently employed in academic studies.
Ring-opening catalysts, mainly Pt-Ir based, were synthesisedat KTH by two different methods: the microemulsion and theincipient wetness methods. Characterization of the catalystswas performed using a number of techniques including TPR,TEM-EDX, AFM and XPS etc. Catalytic screening at atmosphericpressure using pure indan as model substance was utilized todetect ring-opening activity and the magnitude of selectivityto desired cetane-boosting products. The development of suchring-opening catalysts is the topic of Paper I.
When designing a catalytic system aimed at refiningpetroleum, it is crucial to monitor the evolution of thesulphur distribution throughout the different stages of theprocess so that catalyst properties and reaction parameters canbe optimised. The final section of this thesis and Paper II arethus devoted to high-resolution sulphur distribution analysisby means of a sulphur chemiluminescence detector (SCD).
Keywords:ring opening, naphthenes, cetane numberimprovement, indan, light cycle oil (LCO), Pt-Ir catalyst,catalyst characterization, aromatic sulphur compounds, GC-SCD,distribution, analysis.
Murdoch, Alexander. "Structural and compositional analysis of cobalt palladium model catalyst surfaces". Thesis, University of St Andrews, 2012. http://hdl.handle.net/10023/3640.
Testo completoNylén, Ulf. "Ring-opening catalysts for cetane improvement of diesel fuels". Doctoral thesis, KTH, Kemiteknik, 2005. http://urn.kb.se/resolve?urn=urn:nbn:se:kth:diva-537.
Testo completoQC 20101014
Caglar, Basar. "Nox Storage And Reduction Over Ce-zr Mixed Oxide Supported Catalysts". Master's thesis, METU, 2009. http://etd.lib.metu.edu.tr/upload/12610418/index.pdf.
Testo completo#945
-hydroxy carboxylic acid. 10% BaO (w/w) and 1% Pt (w/w) were deposited on synthesized mixed oxide and reference alumina support via incipient wetness impregnation. Prepared catalysts were characterized by BET, XRD and in-situ DRIFTS. Pt/BaO/CexZr1-xO2 catalysts (x= 0.75, 0.5, 0.25) exhibited higher surface than pure ceria and zirconia supported catalysts and highest surface was observed for Pt/BaO/Ce0.5Zr0.5O2. The reducibility of catalysts was tested by Temperature Programmed Reduction (TPR). It was observed that the reducibility of Pt/BaO/CexZr1-xO2 catalysts increases with incorporation of Zr into ceria lattice. Pt/BaO/Ce0.25Zr0.75O2 showed the highest reducibility. The Pt dispersions of catalysts were determined by CO chemisorption. The highest Pt disperison was observed in the presence of Pt/BaO/Ce0.5Zr0.5O2 catalyst. NOx storage and reduction efficiency of the catalysts were determined by transient reaction analysis in a home-built setup at 350oC. The reaction results revealed that all catalysts exhibit similar NOX storage and reduction performance. The NOX storage performances of all catalysts were differentiated via in-situ DRIFTS analysis. Pt/BaO/CexZr1-xO2 (x= 0.75, 0.5, 0.25) catalysts revealed higher performance than the ceria and zirconia supported catalysts. Pt/BaO/Ce0.5Zr0.5O2 catalyst absorbed highest amount of NO on the surface in the form of nitrate. The reduction behaviours of catalysts also were investigated by in-situ DRIFTS. It was observed that nitrates and nitrites were completely removed from the surface after reduction by H2 at 300oC.
Kissounko, Natalia. "Study of dynamics in a reaction catalyzed by ht- and ps-ADH cloning, purification and preliminary x-ray screening /". Access to citation, abstract and download form provided by ProQuest Information and Learning Company; downloadable PDF file, 80 p, 2008. http://proquest.umi.com/pqdweb?did=1605142871&sid=6&Fmt=2&clientId=8331&RQT=309&VName=PQD.
Testo completoHalan, Babu [Verfasser]. "Biofilms as living catalysts for fine chemical synthesis: analysis, process design and scale-up / Babu Halan". Aachen : Shaker, 2013. http://d-nb.info/1051574633/34.
Testo completoNandi, Shreya. "Investigation of perovskite-based three-way catalysts using surface analysis techniques and in situ/operando spectroscopy". Thesis, Lille 1, 2019. http://www.theses.fr/2019LIL1R072.
Testo completoThe catalytic after-treatment of exhaust gases from gasoline engines requires simultaneous abatement of CO, NO and hydrocarbons and is commonly called three-way catalysis (TWC). Perovskites based materials like LaFeO3, regarded as intelligent supports, are being considered as potential candidates as alternative TWC in context of reducing noble metal content. Such bulk catalysts often demonstrate variable surface compositions in comparison to the bulk. Since surface determines the catalytic performance in heterogeneous catalysis, deeper understanding of the surface characteristics especially under relevant reaction conditions becomes imperative. To this end, LaFeO3 based model catalysts relevant to conventional catalysts have been investigated by combination of advanced surface analysis techniques like XPS, LEIS and ToF-SIMS to study the existing surface variations. In addition, catalysts behavior was studied under CO atmosphere by NAP-XPS and GI-XANES. This methodology allowed to reveal that inducing a La-deficiency in the structure helps to improve the catalytic performance due to an interfacial effect. In addition, the different catalytic operating modes of Cu or Mn substituted perovskite powders were determined by in situ/operando Raman spectroscopy
Van, Wyck Neal Edward. "MULTIPHOTON SPECTROSCOPY OF THIN FILMS AND SURFACES (NONLINEAR, WAVEGUIDES, INTERFACES)". Thesis, The University of Arizona, 1985. http://hdl.handle.net/10150/291294.
Testo completoLakhapatri, Satish L. "Analysis of Deactivation Mechanism on a Multi-Component Sulfur-Tolerant Steam Reforming Catalyst". University of Toledo / OhioLINK, 2010. http://rave.ohiolink.edu/etdc/view?acc_num=toledo1279327420.
Testo completoWoo, Jungwon. "Bulk and Surface Characteristics of Model M1 and M2 Phase Catalysts for Propane Ammoxidation to Acrylonitrile". University of Cincinnati / OhioLINK, 2015. http://rave.ohiolink.edu/etdc/view?acc_num=ucin1445615206.
Testo completoAult, Trevor Joseph. "A techno-economic analysis of ethanol production from hydrolysis of cellulose with nanoscale magnetic solid acid catalysts". Kansas State University, 2012. http://hdl.handle.net/2097/14746.
Testo completoDepartment of Chemical Engineering
Keith Hohn
Acid catalysts have been shown to be very successful in the pretreatment of cellulosic biomass to improve glucose yield and improve overall yield of ethanol. This report presents the results of a techno-economic study that looks into the use of nanoscale magnetic solid acid catalysts for glucose production. Magnetic solid acid catalysts are an improvement over using diluted acid due to eliminating acid-waste generation and corrosion hazards. Their magnetic nature also allows them to be easily separated from reaction products by an external magnetic force. After the technology is analyzed, a series of unit operations is proposed to go from the laboratory scale to the industrial plant scale. The next step was to develop material and energy balances using HYSYS process simulation software. Capital and operating costs are estimated and all the information is combined into a discounted cash flow economic model. The economic portion of the report uses a probabilistic cost assessment. It is used to quantify the range of risks in the project from swings in feedstock costs, differences in yield from catalysts, and any other significant variables. Both capital costs (initial equipment & construction investment) and operating costs (feedstock supply, chemicals, and personnell) are included with ranges of error based on databases and expert opinion. This method of evaluating investment efficiency can be helpful for predicting the cost benefits of proposed future research. The yield and percent catalyst magnetically recovered is assumed based on laboratory research to simplify the model. A 2000 metric tons of biomass per day facility was analyzed. Using the magnetic solid acid catalyst technology, the capital costs are estimated to be $160 million and this technology saves around 10% of capital costs compared to ethanol plants that uses conventional acid hydrolysis. The yield of the magnetic solid acid catalysts should be around 75% to compete with existing ethanol technologies. The metric used for this report is the discount profitability index (DPI) which is the ratio of future cash flows divided by investment. A DPI “hurdle rate” of 1.3 is used, which is similar to industry economic metrics of projects that include new process plants. The calculated DPI for the project is 1.38 DPI which is higher than using conventional cellulose treatment technologies. The recommendation is continue to study this technology’s large scale applicability before attempting any plant pilot studies.
Wei, Bo. "A novel solar-driven system for two-step conversion of CO2 with ceria-based catalysts". Doctoral thesis, KTH, Kraft- och värmeteknologi, 2014. http://urn.kb.se/resolve?urn=urn:nbn:se:kth:diva-152899.
Testo completoQC 20141006
Wang, Meng. "Steam reforming of model compounds of bio-oil with and without CO₂ sorbent". HKBU Institutional Repository, 2014. https://repository.hkbu.edu.hk/etd_oa/212.
Testo completoVillaseñor, Milán Ángela. "Development and optimization of methods for elemental quantitative analysis of catalysts and polymers through laser ablation-ICP techniques". Doctoral thesis, Universidad de Alicante, 2018. http://hdl.handle.net/10045/97855.
Testo completoAlston, Ben. "Aqueous polyoxometalates : design and analysis of electrochemical catalysts for the indirect reduction of oxygen in PEM fuel cells". Thesis, University of Liverpool, 2013. http://livrepository.liverpool.ac.uk/16233/.
Testo completoReineri, Daniele. "Síntese e caracterização dos coprecipitados de cálcio e alumínio com 8-hidroxiquinolina e avaliação catalítica na reação de transesterificação". Universidade Tecnológica Federal do Paraná, 2015. http://repositorio.utfpr.edu.br/jspui/handle/1/1504.
Testo completoThe present study aimed to synthesize and evaluate the activity catalytic in the reaction transesterification of the material formed after decomposition thermal of coprecipitated of calcium and aluminum with 8-hydroxyquinoline. The synthesis of the material was performed by method coprecipitation using as agent precipitating 8-hydroxyquinoline. To evaluate the presence of metal calcium and aluminum on the characteristics of the material, we used different percentages of these metals in the synthesis of complexes using the same conditions reaction, with a pH final of 10 to temperature of 25 ºC. After synthesis the complexes were characterized by scanning electron microscopy, infrared spectroscopy, and thermal analysis in synthetic air atmosphere at heating rates of 5 °C, 10 °C and 20 ºC min-1. Through the curves TG, DTA and DTG was found that the presence of metal aluminum promoted process partial of sublimation the material. The materials obtained after analysis thermal were characterized by scanning electron microscopy, not observed changes significant in morphology between the different reasons heating. For review catalytic on reaction transesterification used a ratio molar of acetate ethyl:methanol 1:6, temperature 50 °C, time reaction 1 hour to 1% catalyst, the catalyst being obtained at temperature a calcination of 700 °C with a rate heating 10 ºC min-1. The highest conversion (0.98%) was obtained from the material synthesized with 100% metal calcium in its formulation, but the conversions are low seen partially due to the conditions mild used.
Butts, Robert Andrew. "Kinetic parameters from statistical analysis of TREF profiles and the preparation of MgCl¦2 as supports for polymerization catalysts". Thesis, National Library of Canada = Bibliothèque nationale du Canada, 2000. http://www.collectionscanada.ca/obj/s4/f2/dsk1/tape3/PQDD_0011/MQ60106.pdf.
Testo completoBrown, Jared C. "UV Visible Spectra Analysis of High Temperature Water Gas Shift Catalysts Made from Iron, Lanthanum, Copper, and Chromium Oxides". BYU ScholarsArchive, 2012. https://scholarsarchive.byu.edu/etd/3222.
Testo completoRankin, Andrew Gordon McLaughlin. "Applications of multinuclear solid-state NMR spectroscopy to the characterisation of industrial catalysts". Thesis, University of St Andrews, 2018. http://hdl.handle.net/10023/12793.
Testo completoKaramullaoglu, Gulsun. "Dynamic And Steady-state Analysis Of Oxidative Dehydrogenation Of Ethane". Phd thesis, METU, 2005. http://etd.lib.metu.edu.tr/upload/12606269/index.pdf.
Testo completoand the small Cr2O3 and V2O4 phases of Cr-V-O were revealed. In H2-TPR, both catalysts showed reduction behaviour. From XPS the likely presence of Cr+6 on fresh Cr-O was found. On Cr-V-O, the possible reduction of V+5 and Cr+6 forms of the fresh sample to V+4, V+3 and Cr+3 states by TPR was discovered through XPS. With an O2/C2H6 feed ratio of 0.17, Cr-O exhibited the highest total conversion value of about 0.20 at 447°
C with an ethylene selectivity of 0.82. Maximum ethylene selectivity with Cr-O was obtained as 0.91 at 250°
C. An ethylene selectivity of 0.93 was reached with the Cr-V-O at 400°
C. In the experiments performed by using CO2 as the mild oxidant, a yield value of 0.15 was achieved at 449°
C on Cr-O catalyst. In dynamic experiments performed over Cr-O, with C2H6 pulses injected into O2-He flow, the possible occurrence of two reaction sites for the formation of CO2 and H2O was detected. By Gaussian fits to H2O curves, the presence of at least three production ways was thought to be probable. Different from Cr-O, no CO2 formation was observed on Cr-V-O during pulsing C2H6 to O2-He flow. In the runs performed by O2 pulses into C2H6-He flow over Cr-V-O, formation of CO rather than C2H4 was favored.
Sen, Fatih. "The Preparation And Analysis Of New Carbon Supported Pt And Pt+second Metal Nanoparticles Catalysts For Direct Methanol Fuel Cells". Phd thesis, METU, 2012. http://etd.lib.metu.edu.tr/upload/12614728/index.pdf.
Testo completoC, 300 °
C, and 400 °
C for 4 h under argon gas. Lastly, PtRu/C catalysts, which have different atomic percent ratios of Pt and Ru (Pt/Ru: 0.8, 2.1 and 3.5), were prepared using PtCl4 and RuCl3 as starting materials and tert-octanethiol as a surfactant. Each was characterized by X-ray diffraction, transmission electron microscopy, energy dispersive analysis, X-ray photoelectron spectroscopy, cyclic voltammetry, and elemental analysis, and their activities were determined toward the methanol oxidation reaction. It has been found that all prepared catalysts are more active toward methanol oxidation reaction compared to the commercial catalysts. It was also found that increasing the temperature during the heat treatment process results in an enlargement of platinum particle size and a decrease in catalytic activity in the methanol oxidation reaction. Transmission electron microscopy shows that platinum nanoparticles are homogeneously dispersed on the carbon support and exhibited a narrow size distribution with an average particle size of about 2-3 nm in diameter. X-ray photoelectron spectra of all catalysts indicated that most of the platinum nanoparticles (>
70 %) have an oxidation state of zero and rest (<
30 %) have a +4 oxidation state with (Pt 4f7/2) binding energies of 71.2-72.2 and 74.3-75.5 eV, respectively.
Song, Hua. "Investigation of Reaction Networks and Active Sites in Bio-ethanol Steam Reforming over Cobalt based Catalysts". The Ohio State University, 2009. http://rave.ohiolink.edu/etdc/view?acc_num=osu1243999804.
Testo completoShirvani, Tara. "The role of catalysts and algae in forming a sustainable solution for a global food and fuel crisis". Thesis, University of Oxford, 2012. http://ora.ox.ac.uk/objects/uuid:30af0957-1ed6-4ea7-949b-f120606ab22e.
Testo completoNaidoo, Preloshni. "A comparative analysis of the chemical composition of linear low density polyethylene polymers synthesised with 1- hexene comonomer under different catalytic conditions". Thesis, Stellenbosch : Stellenbosch University, 2013. http://hdl.handle.net/10019.1/80272.
Testo completoENGLISH ABSTRACT: A comparative study of the chemical composition of linear low density polyethylene polymers, synthesised with 1 - hexene as comonomer was conducted. Catalyst trials were conducted on the linear low density 1 - hexene polymer grade material to evaluate alternative catalysts. A comparative analysis was performed in order to investigate if the samples synthesised under catalyst trial conditions showed any significant differences in terms of crystallinity and mechanical properties with the reference sample that was synthesised using the reference catalyst. The results showed that the macro product properties, namely melt flow Index, density, and level of hexene extractables are different for the trial samples in comparison with the reference sample. The differences observed implied that the trial samples were synthesised with differences on a molecular level. The differences in the chemical composition between the reference sample and the comparative samples were fully explored using a wide range of analytical techniques, namely crystallisation analysis by fractionation (CRYSTAF), temperature rising elution fractionation (TREF), differential scanning calorimetry (DSC), Carbon 13 nuclear magnetic resonance (13C NMR), Size exclusion chromatography (SEC), Positron analysis lifetime spectroscopy (PALS) and micro hardness analysis. The results of the characterisation studies indicated the following: - Crystallinity and hardness analysis of the reference sample, catalyst trial sample 1 and catalyst trial sample 2 indicate that the catalyst trial sample 2 having a low cocatalyst concentration is the most crystalline of all the samples. - The reference sample, catalyst trial sample 1 and catalyst trial sample 2 were further fractionated using TREF at fractionation temperature intervals of 10°C. TREF analysis indicates that the bulk of the material is observed to elute between 70°C - 10°C. - 13C NMR analyses of the TREF fractions identified four populations of fractions that could be selectively removed, allowing the bulk of the material to be recombined. As these highly crystalline fractions were removed, there was an observed decrease in the total crystallinity of the bulk recombined material. This trend was further verified by the free volume analysis. - Free volume analysis indicated of the bulk recombined material indicated a general increase in the T3 lifetime and T4 lifetime intervals. Free volume analysis further confirmed a decrease in crystallinity of the bulk recombined material as highly crystalline material was removed. - Micro hardness analysis of the polymers further verified the crystallinity trends observed. As the molecular composition of the polymer changed due to removal of highly crystalline fractions, the total mechanical strength of the material indicated by the hardness value decreased. The study showed that by changing the chemical composition of the polymer by removing highly crystalline fractions, there was an observed change in the mechanical properties of the polymer. It can be concluded that the samples synthesised under catalyst trial conditions show significant differences in terms of crystallinity and mechanical properties in comparison with the sample that was synthesised using the standard reference catalyst.
AFRIKAANSE OPSOMMING: ‘n Vergelykende analise studie is onderneem van die chemiese samestellings van lineêre lae digtheid poliëtileen polimere, gesintetiseer met 1-hekseen as ko-monomeer. Alternatiewe kataliste is ge-evavuleer ten opsigte van lineêre lae digtheid 1-hekseen Sasol polimeer graad materiaal. Die vergelykende analise is uitgevoer om die monsters onder katalis proef kondisies te evalueer en te merk of enige beduidende verskille in terme van kristalliniteit en meganiese eienskappe met die verwysings monster voorkom. Die resultate toon dat die makro-produk eienskappe, naamlik smelt vloei indeks, digtheid en vlak van hekseen onttrekking, verskillend is vir die proef monsters in vergelyking met die verwysings monster. Die waargenome verskille impliseer dat die proef monsters op molekulêre vlak verskil. Die verskille in chemiese samestelling tussen die verwysings monster en die vergelykende monsters is ten volle ondersoek deur gebruik te maak van 'n wye verskeidenheid van analitiese tegnieke, naamlik kristallisasie analise fraksionering (CRYSTAF), temperatuur stygende eluering fraksionering (TREF), differensiële skandeer kalorimetrie (DSC), koolstof 13 kernmagnetiese resonansie (13C KMR), gelpermeasie chromatografie (SEC), positron analise leeftyd spektroskopie (PALS) en mikro-hardheid analise. Die resultate van die karakterisering studies het die volgende aangedui:- Kristalliniteit en hardheid analises van die verwysings monster en katalis proef monsters 1 en 2 het getoon dat katalis proef monster 2, wat ‘n lae ko-katalis konsentrasie bevat, die mees kristallyn is. - Die verwysings monster en katalis proef monster 1 en 2 is gefraksioneer met behulp van ‘n TREF met temperatuur tussenposes van 10°C. TREF analise toon dat oormaat materiaal ge-elueer word tussen 70°C en 100°C. - 13C KMR analise van die TREF fraksies het 4 verskillende fraksies geidentifiseer wat selektief verwyder kan word. Dit laat ook toe dat die grootste deel van die materiaal weer geherkombineer kan word. Soos die hoogs kristallyne fraksies verwyder is, is ‘n afname in die totale kristalliniteit van die geherkombineerde materiaal waargeneem. Hierdie tendens is bevestig deur vrye volume analises. - Vrye volume analises van die geherkombineerde materiaal toon ‘n algemene toename in die T3en T4 leeftyd aan. Vrye volume analises toon verder dat ‘n afname in die kristalliniteit van die geherkombineerde materiaal plaasvind soos meer kristallyne fraksies verwyder word. - Verdere mikro-hardheid analises van die polimere bevestig die waargenome kristalliniteit tendense. Soos die molekulêre samestelling van die polimere verander as gevolg van die verwydering van die hoogs kristallyne fraksies, so neem die totale meganiese sterkte van die materiaal af; soos aangedui deur die afname in hardheid waarde. Die studie toon dat die verandering van die chemiese samestelling van die polimeer, deur die verwydering van hoogs kristallyne fraksies, 'n waargenome verandering in die meganiese eienskappe van die polimeer laat plaasvind. Daar kan afgelei word dat die monsters, vervaardig onder die katalis proef voorwaardes, beduidende verskille toon in terme van kristalliniteit en meganiese eienskappe in vergelyking met die monster vervaardig deur die huidige verwysings katalis.
MacArthur, Katherine E. "Quantitative structural and compositional characterisation of bimetallic fuel-cell catalyst nanoparticles using STEM". Thesis, University of Oxford, 2015. http://ora.ox.ac.uk/objects/uuid:6ce29b0c-1e7e-4604-ba5b-22f2ebd03d4e.
Testo completoWang, Xingli [Verfasser], Peter [Akademischer Betreuer] Strasser, Frédéric [Gutachter] Jaouen e Peter [Gutachter] Strasser. "Copper-based nanostructured catalysts for efficient and selective CO2 electroreduction – synthesis, catalytic performance, and mechanistic analysis / Xingli Wang ; Gutachter: Frédéric Jaouen, Peter Strasser ; Betreuer: Peter Strasser". Berlin : Technische Universität Berlin, 2020. http://d-nb.info/1209601494/34.
Testo completoStokoe, Robert B. "Conformational and mechanistic studies on asymmetric cyanohydrin synthesis : an analysis of the dipeptide catalysts cyclo-[(S)-His-(S)-Phe], cyclo-[(S)-His-(S)-Leu] and related compounds". Thesis, Bangor University, 1996. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.320398.
Testo completoROCHA, SORAYA M. R. da. "Síntese e caracterização de precursores para catalisadores termicamente estáveis à base de lantanideos pelo método sol-gel". reponame:Repositório Institucional do IPEN, 2005. http://repositorio.ipen.br:8080/xmlui/handle/123456789/11271.
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Tese (Doutoramento)
IPEN/T
Instituto de Pesquisas Energeticas e Nucleares - IPEN/CNEN-SP
SILVA, SIRLANE G. da. "Estudo do efeito do suporte em catalisadores de Cobalto e Níquel para obtenção de Hidrogênio a partir da reforma a vapor do etanol". reponame:Repositório Institucional do IPEN, 2013. http://repositorio.ipen.br:8080/xmlui/handle/123456789/10177.
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Dissertação (Mestrado)
IPEN/D
Instituto de Pesquisas Energeticas e Nucleares - IPEN-CNEN/SP
Kováč, Martin. "Katalyzátory pro kladnou elektrodu kyslíko-vodíkového palivového článku". Master's thesis, Vysoké učení technické v Brně. Fakulta elektrotechniky a komunikačních technologií, 2010. http://www.nusl.cz/ntk/nusl-218699.
Testo completoHaire, Andrew Richard. "Probing the influence of bimetallic composition on the Pd/Au catalysed synthesis of vinyl acetate monomer". Thesis, University of St Andrews, 2010. http://hdl.handle.net/10023/1018.
Testo completoLundgren, Stina. "Efficient Synthesis and Analysis of Chiral Cyanohydrins". Doctoral thesis, Stockholm : Kungliga Tekniska högskolan (KTH), 2007. http://urn.kb.se/resolve?urn=urn:nbn:se:kth:diva-4315.
Testo completoKebe, Seydina Ibrahima. "Synthèse de matériaux monolithiques pour la séparation et la catalyse en phase liquide : problématiques environnementales et du développement durable". Thesis, Paris Est, 2016. http://www.theses.fr/2016PESC1127/document.
Testo completoPolymeric materials have gained immense popularity with the golden age of petroleum and they still today meet with great success through Green polymer chemistry approaches and numerous high added value dedicated application in scientific domains such as analytical chemistry, medicine, space investigations, where one of the key for success is the design of miniaturized objects. In this contribution, micro-sized monolithic materials have been designed though either in microchannel immobilization (I.D. = 75 µm) or surface attachment on glass substrates (hundredths of microns in thickness). Polymers exhibiting monolithic morphology were considered to benefit of high permeability, mechanical and thermal resistances which are mandatory to flow chemistry applications. With the aim to control the interfacial interaction ability, a generic monolith having N-hydroxysuccinimide ester groups was used and on purpose functionalized. Molecular segments acting as selector – for electrochromatographic applications – of metal nanoparticles ligands – for supported catalysis applications – have been immobilized on the monolith surface via classical (nucleophilic substitution) or original (photo-induced thiol-ene click) grafting reactions.The so-designed materials were characterized through spectroscopic, microscopic, diffraction, thermogravimetric methods providing insight into correlation between the observed separation and catalytic abilities and the interfacial structure of the monolith. As representative examples of application, one may cite the electrochromatographic separation of toxic molecules such as organic pollutants (phenols, anilines, polycyclic aromatic hydrocarbons, polychlorobiphenyls), preservatives in cosmetics (parabens) and biomarkers (polycyclic aromatic hydrocarbons, pyrimidic bases). The analyses were conducted on model solutions and complex matrices (cosmetics, extraterrestrial analog samples). Flow catalytic reaction meant for the reduction of nitroarenes, the oxidation of aromatic alcohol, the carbon-carbon coupling and the sensitive detection of pesticides and synthesis intermediates (para-nitrophenol) have been achieved
Reece, Christian. "Kinetic analysis and modelling in heterogeneous catalysis". Thesis, Cardiff University, 2017. http://orca.cf.ac.uk/103737/.
Testo completoAutin, Laura. "Étude des cinétiques de réticulation et de la dynamique moléculaire de réseaux silicones : compréhension des mécanismes catalytiques par analyse viscoélastique et RMN". Thesis, Lyon 1, 2012. http://www.theses.fr/2012LYO10258.
Testo completoSilicones condensation catalysis, and more especially room temperature vulcanizable compounds, is a very important scientific, environmental and economic issue. The catalysis species, derivated from tin dilaurate, which are now classified as a CMR2 compound (toxic for reproduction), have been widely used in the silicone industry. The new REACH regulation is going to forbid its use very soon. This study aims to work on new catalytic systems. The influence of the components of the formulation on the kinetics and mechanical properties has been study by different methods: rheology, NMR and swelling measurements. More precisely, this work focuses on two catalysts: one guanidine and zinc complexes. Results have shown that the network construction depends on the catalysis. In fact, while using a tin compound, the construction occurs in two steps, in which hydrolysis is the most important. As a comparison, zinc complexes present the same behaviour as tin compounds even though the hydrolysis step is much more important. On the contrary, it’s known that basic catalysis enhances the condensation step. Then, the guanidine quickly reacts with the silanol functions. Then, in a second step, the alkoxysilanes hydrolysis occurs in a smaller proportion. The tridimensional network is getting built. This work mainly showed that zinc complexes can easily replace tin compounds
Penkala, Bartosz. "Low Temperature Oxygen Mobility Applied to Catalysis". Thesis, Montpellier, 2015. http://www.theses.fr/2015MONTS022.
Testo completoAccomplishing specifications of new regulations regarding automotive exhaust after-treatment technologies, e.g. TWC, imply the availability and usage of catalytically active materials and especially oxygen buffer compounds, which can reversibly store and release high quantities of the oxygen. Doped cerium oxide presents still today the only reference compound for a suitable support, due to its high oxygen storage capacity and ability to easily create oxygen ion vacancies. However, for economic reasons and very limited natural abundance to a few countries, the substitution of ceria appears to be mandatory; in this context we note that ceria is part of the list of 13 economically important raw materials which were identified by the European Commission as subject to a high risk of supply interruption.In this context, Brownmillerite-type oxides are of potential interest, since they reveal oxygen ion mobility down to ambient temperature. Furthermore, they allow to adjust the presence of extended defects e.g. anti-phase boundaries, during synthesis conditions, and which have been shown to significantly decrease the activation energy for oxygen diffusion. We were thus able to show that defect-rich nano-Ca2Fe2O5, traditionally known as a stoichiometric line-phase, can be oxidized under mild conditions to CaFeO3, while the oxidation of ordinary Ca2Fe2O5 usually requires extreme reaction conditions, i.e. 1100°C and several GPa oxygen partial pressure. Thus, introducing a high concentration of defects seems to be a promising concept to transform even traditionally known stoichiometric line-phases to become a kind of oxygen sponge and behave as oxygen storage/buffer compound at very moderate temperatures. This behavior is thus comparable to the oxygen storage capacity of doped cerium oxide, and offers a true potential for application in the catalysis. Consequently, the Brownmillerite Ca2Fe2O5 appears to be a promising candidate to study due to its known oxygen ion conductivity properties.Primary aim of this work is to establish fundamental relation between structure/microstructure, oxygen mobility properties and catalytic activity, simultaneously undertaken for two systems: Ca2Fe2O5 with Brownmillerite-type structure and CeO2 with Fluorite-type structure. We essentially explored the underlying criteria governing their chemical/catalytic activity, using oxygen isotope exchange behavior by TG couples MS experiments. Further studies using essentially Raman spectroscopy allowed concluding from a modified lattice dynamics for different oxygen isotopes to differentiate between bulk and surface oxygen participation to the oxidation mechanism of CO to CO2. For a deeper mechanistic understanding of the CO oxidation, we developed a new catalytic test, based on a dynamic variation of the oxygen partial pressure in the reaction vessel, allowing to conclude simultaneously on the catalytic activity of the catalyst and its oxygen release/uptake behavior, not accessible by the classical catalytic activity test performed under constant gas flow. In this way we got a new insight to differentiate the participation of surface and bulk oxygen activity for different Ca2Fe2O5 and ceria based catalysts
Margeriat, Alexandre. "Conversion catalytique des vapeurs de pyrolyse et molécules modèles". Thesis, Lyon, 2017. http://www.theses.fr/2017LYSE1340/document.
Testo completoFast pyrolysis of biomass yields bio-oils with high levels of oxygen-containing components, high acidity and low stability. Further upgrading of these oils is necessary before they can be used as liquid fuels. Several low-cost strategies have been proposed for reducing the oxygen and acid contents including the catalytic conversion of pyrolytic vapors before vapor condensation. In this context, a first step in this work was the study of model molecules conversion, acetic acid and guaiacol, on different acid catalyst to understand reaction mechanisms and determine the best catalyst. In a second time, a semi-continuous pyrolysis test combined with a catalytic reactor was built and use to test the best acid catalysts found on model molecules, for the conversion of beech wood chips. A product recovery protocol was implanted to recover all the gas, liquid and solid fractions. Those fractions were characterized in depth by various techniques (?-GC, GC×GC, GPC, RMN…). A special focus was made on the quantification of monomers in the bio-oils by GC×GC. Mass balance reached 90% and carbon balance were established for some experiments. The performed characterizations as well as the comparison between catalytic and thermal experiments allowed to get more insights in the role of the catalyst on pyrolytic vapors conversion