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Wyszukujesz frazę "oxide catalyst" wg kryterium: Wszystkie pola


Tytuł:
Application of Kelvin method and mass spectrometry for investigation of oxide catalyst surface properties
Autorzy:
Maniak, G.
Stelmachowski, P.
Powiązania:
https://bibliotekanauki.pl/articles/115729.pdf
Data publikacji:
2010
Wydawca:
Fundacja na Rzecz Młodych Naukowców
Tematy:
work function
Kelvin method
mass spectrometry
oxide catalyst
N2O decomposition
Opis:
Many oxides are applied as a catalysts for commercially important processes. Recently, decomposition of nitrous oxide into nitrogen and oxygen have became a topic of vital interest for catalytic chemistry. Two possible ways of deN2O reaction, low temperature and high-temperature, can be distinguished. Promising results were obtained for spinel oxides which contained cobalt. Because of cationic redox route, triggered by electron transfer, of N2O decomposition over these oxides, investigation of their electronic properties was justifi ed. Th erefore the work function measurements, using Kelvin method were carried out. Moreover in-situ monitoring of processes occurred at catalyst’s surface was performed using mass spectrometry.
Źródło:
Challenges of Modern Technology; 2010, 1, 1; 11-13
2082-2863
2353-4419
Pojawia się w:
Challenges of Modern Technology
Dostawca treści:
Biblioteka Nauki
Artykuł
Tytuł:
Promoted cobalt oxide catalyst on the metallic structured reactor filling for VOC combustion as an alternative to noble metal catalysts
Autorzy:
Łojewska, J.
Kołodziej, A.
Żak, J.
Powiązania:
https://bibliotekanauki.pl/articles/778425.pdf
Data publikacji:
2007
Wydawca:
Zachodniopomorski Uniwersytet Technologiczny w Szczecinie. Wydawnictwo Uczelniane ZUT w Szczecinie
Tematy:
technika Langmuira-Blodgett
nośnik strukturalny
mikroskopia Ramana
analiza ilościowa
Langmuir-Blodgett technique
structured carrier
wash-coat layer
Raman microscopy
XPS quantitative analysis
Opis:
VOC combustion is a demanding process for both the reactor and the catalyst design. As we have proved in recent papers the diffusional limitation of reaction rate that occurs during combustion may be overcome by designing the metallic microstructures used as reactor internals. Their application on an industrial scale depends on the development of an efficient method of catalyst layering on metallic supports and the optimisation of a fine catalyst structure which would not change the elaborated microstructure geometry. In this study we propose the Langmuir-Blodgett (LB) film method to deposit various metals (Al, Co) in the form of catalyst organic precursors. The film forming abilities of the precursors were checked by surface pressure measurements upon film compression, Brewster Angle Microscopy and by the monolayers stability measurements. The amount of the deposited materials was controlled by the LB parameters and verified by the TG measurements. The catalyst obtained in this way were characterized at various stages of the preparation by SEM/XFS, XPS, AFM and RM methods and tested in n-hexane combustion. Oxidation of the Al washcoat precursor led to the formation of γ-Al2O3 improving the properties of the Al2O3 layer (α phase) developed on the pre-calcined CrAl carrier. Oxidation of cobalt stearate deposited on the CrAI produced dispersed Co3O4 spinel. The cobalt catalysts were active in combustion showing resistance to sintering. Compared to standard Pt supported catalyst it demonstrated twice as low activation energy (50 kJ/mol).
Źródło:
Polish Journal of Chemical Technology; 2007, 9, 1; 15-19
1509-8117
1899-4741
Pojawia się w:
Polish Journal of Chemical Technology
Dostawca treści:
Biblioteka Nauki
Artykuł
Tytuł:
Estimation of the oxide catalyst volume and the cells quantity influence on CO, HC and NOx conversion in the AVL boost computing application
Autorzy:
Kruczyński, S.
Kamela, W.
Duniec, K.
Powiązania:
https://bibliotekanauki.pl/articles/242900.pdf
Data publikacji:
2012
Wydawca:
Instytut Techniczny Wojsk Lotniczych
Tematy:
combustion engines
catalytic reactors
simulation
air pollution
environmental protection
Opis:
The article contains the results of the simulation tests of oxidizing catalytic reactor obtained by use of the AVL Boost simulation application. The chemical reactions and the reactions rates on which computations were based are specified in this paper. The simulations were related to the influence of the catalytic reactor volume and reactor’s cells quantity influence on the carbon oxide, hydrocarbons and nitric oxides conversion levels. The influence on the nitric oxides conversion was presented in this paper as the content of NO and NO2 in NOX. The simulated computations were performed separately for the variable reactor volume ranging from 1 to 2.2 dm3 with a step of 0.4 dm3 and for the variable reactor cells quantity ranging from 200 to 600 cells per square inch with a step of 100 cpsi. As the input data for the simulation computations the actual values of the toxic compounds concentrations in the exhaust gases at the outlet of the Diesel engine were used. The measurements of the toxic compounnds were made at the chosen engine steady state work points and are presented in this paper as a graph of the toxic gases concentrations in the form of the function of the engine torque. The simulation computaitons were performed for the same points and their results are also presented in the form of the function of the engine torque. The Results presented in this paper have shown that the increase in the CO, HC and NOX conversion in the case of the oxide catalyst can be obtained both by increasing the reactor volume and its cells quantity. It also have been observed that the increase in the reactor cells quantity and volume is not proportional as regards the toxic gases conversion increase and lowers in the case of higher values of the simulated reactor parameters.
Źródło:
Journal of KONES; 2012, 19, 4; 347-353
1231-4005
2354-0133
Pojawia się w:
Journal of KONES
Dostawca treści:
Biblioteka Nauki
Artykuł
Tytuł:
Ozone decomposition on ZnO catalysts obtained from different precursors
Autorzy:
Milenova, Katya I.
Nikolov, Penko M.
Kasabova, Nikoleta A.
Avramova, Ivalina A.
Powiązania:
https://bibliotekanauki.pl/articles/778353.pdf
Data publikacji:
2014
Wydawca:
Zachodniopomorski Uniwersytet Technologiczny w Szczecinie. Wydawnictwo Uczelniane ZUT w Szczecinie
Tematy:
ozone decomposition
zinc oxide catalyst
manganese doping
copper doping
nanosize
Opis:
Kinetic investigations for ozone conversion on three different series of zinc oxide catalysts, containing pure ZnO and doped with Mn or Cu one with dopant content less than 1 wt.% were carried out. The different samples were obtained from carbonate, nitrate and acetate precursors. The as prepared catalysts were characterized by AAS, XRD, IR, EPR and BET methods. The mean size of the crystallites determined by XRD data is in the range 27÷68 nm. The presence of Mn2+ and Cu2+ ions into the ZnO matrix was established by EPR. The ozone decomposition was investigated for 30÷75°C temperature range. The zinc carbonate precursor samples show highest activity, while the nitrate precursor ones show lowest activity toward reaction decomposition of ozone in the whole temperature range. At 75°C two of the catalyst, obtained from carbonate precursor - ZnO and CuZnO show 100% conversion.
Źródło:
Polish Journal of Chemical Technology; 2014, 16, 4; 55-59
1509-8117
1899-4741
Pojawia się w:
Polish Journal of Chemical Technology
Dostawca treści:
Biblioteka Nauki
Artykuł
Tytuł:
Synthesis and activity evaluation of Ce-Mn-Cu mixed oxide catalyst for selective oxidation of co in automobile engine exhaust: effect of Ce/Mn loading content on catalytic activity
Autorzy:
Bilal, Yasir
Nasir, Muhammad Ali
Nasreen, Sadia
Akhter, Niaz Ahmed
Pasha, Riffat Asim
Noor, Muhammad Farhan
Powiązania:
https://bibliotekanauki.pl/articles/101992.pdf
Data publikacji:
2018
Wydawca:
Stowarzyszenie Inżynierów i Techników Mechaników Polskich
Tematy:
base metal oxide catalyst
catalytic converter
CO sensor
CO-precipitation
catalytic activity
katalizator tlenku metalu zasadowego
katalizator
czujnik CO
strącanie CO
aktywność katalityczna
Opis:
A series of Mn-doped CeO2-CuO catalyst (CeO2-MnOx-CuO) (Ce/Mn molar ratio of 0.5, 1.0 2.0 and 3.0) were prepared using co-precipitation method for the selective oxidation of CO in automobile engine exhaust. The content of copper was 5.0 wt. % in each sample. Catalysts were installed on the automobile engine exhaust and CO amount was recorded with help of CO sensor, with and without the catalyst. The catalytic converter efficiency was estimated for each catalyst through efficiency formula. It was observed that Ce/Mn catalyst with a molar ratio of 2.0 shows the maximum efficiency (88.35%). Stability of conversion process was analyzed by plotting the CO amount with respect to time. The catalyst with Ce/Mn molar ratio of 2.0 performed the most streamline conversion process with least deviations.
Źródło:
Advances in Science and Technology. Research Journal; 2018, 12, 1; 260-266
2299-8624
Pojawia się w:
Advances in Science and Technology. Research Journal
Dostawca treści:
Biblioteka Nauki
Artykuł
Tytuł:
Optimization of an active phase composition in the low-temperature nitric oxide reduction catalyst
Autorzy:
Kułażyński, M.
Bratek, K.
Walendziewski, J.
Powiązania:
https://bibliotekanauki.pl/articles/777954.pdf
Data publikacji:
2007
Wydawca:
Zachodniopomorski Uniwersytet Technologiczny w Szczecinie. Wydawnictwo Uczelniane ZUT w Szczecinie
Tematy:
NOx
SCR
katalizator
optymalizacja
nośnik mineralno-węglowy
catalyst
optimization
mineral-carbon carrier
Opis:
In the first research studies series a selection of the quantitative composition of catalyst active phase composition (iron, copper and manganese) deposited on mineral-carbon support was carried out. It was found on the basis of the selection studies series that the best results were attained when copper and manganese were used as catalyst components. The quantitative composition of the denitrogention catalyst was estimated using a statistical method of experiment planning and metals content changed in the range 0.5 - 1.5wt % for both metals. Catalyst activity in nitric oxide reduction by ammonia was determined in the dependence on an active phase composition in the temperature range 100 - 200° C, at GHSV (Gas Hour Space Velocity) 6 000 and 10 000 Nm3/m3h, NO concentration 400 ppm, NH3/NO ratio 1:1. A graphic presentation of the obtained results was made using the UNIPLOT program. The highest activity in nitric oxide reduction by ammonia presented copper - manganese catalysts prepared by the impregnation of mineral-carbon support with active metals salts solutions and calcination after each metal impregnation with copper (up to 1.5 wt %) and manganese (up to 1.5 wt %).
Źródło:
Polish Journal of Chemical Technology; 2007, 9, 3; 33-37
1509-8117
1899-4741
Pojawia się w:
Polish Journal of Chemical Technology
Dostawca treści:
Biblioteka Nauki
Artykuł
Tytuł:
Ograniczenie emisji metanu z kopalń węglowych poprzez katalityczne oczyszczanie powietrza wentylacyjnego
Autorzy:
Stasińska, B.
Powiązania:
https://bibliotekanauki.pl/articles/283453.pdf
Data publikacji:
2009
Wydawca:
Polska Akademia Nauk. Instytut Gospodarki Surowcami Mineralnymi i Energią PAN
Tematy:
katalityczne utlenianie metanu
spalanie płomieniowe metanu
katalizatory palladowe
wykorzystanie metanu
methane catalytic oxidation
flameless methane combustion
oxide catalyst
palladium catalysts
methane utilization
Opis:
Praca proponuje katalityczne utlenianie metanu jako rozwiązanie problemu emisji metanu, gdy jego stężenie uniemożliwia spalanie płomieniowe. Wskazuje źródła emisji metanu takie jak kopalnie węgla, które powiększają efekt cieplarniany przez ciągłą emisję metanu w niewielkich stężeniach. Użycie katalitycznego utleniania metanu pozwoli na jego utlenienie przy stężeniach uniemożliwiających zapłon i zależnie od rozwiązania technologicznego może być sposobem przyjaznego środowisku pozyskiwania energii elektrycznej i cieplnej lub tylko metodą utylizacji metanu.
Ventilation air is a difficult source of methane to use as an energy carrier, as air volume is large, methane is very diluted as well as variable in its concentration (0.1–1.0 vol.%) and flow rate. The paper indicates the coal mines as a source of the permanent emission of low-concentrated methane, which have increased the greenhouse effect. This paper proposes the catalytic oxidation of methane as the solution for the problem of methane utilization when its concentration in air is insufficient for flame combustion. The studies conducted for many years have enabled to find the active oxide and metallic catalytic systems for the reaction of methane oxidation. For the utilization of gases with low-concentrated methane it seems to be economically well-justified to use of the low-temperature catalysts, especially palladium catalysts. Depending on technological solutions it can be considered as a method for methane utilization or as an environmentally friendly way for generation of electric and thermal energy.
Źródło:
Polityka Energetyczna; 2009, T. 12, z. 2/1; 123-132
1429-6675
Pojawia się w:
Polityka Energetyczna
Dostawca treści:
Biblioteka Nauki
Artykuł
Tytuł:
Estimation of nox conversion into oxide, platinum and combined oxide - platinum SCR catalyst
Autorzy:
Kamela, W.
Kruczyński, S.
Powiązania:
https://bibliotekanauki.pl/articles/246547.pdf
Data publikacji:
2012
Wydawca:
Instytut Techniczny Wojsk Lotniczych
Tematy:
combustion engines
catalytic reactors
selective reduction
nitric oxides
air pollution
Opis:
The paper contains the results of the tests of the oxide, platinum and combined oxide-platinum catalytic reactor model used in the NH3-SCR system. As regards the combined oxide-platinum catalyst the first reactor block was extracted from the oxide catalyst used in trucks. As the second module of the reactor a block with platinum acting as a catalyst was used with 2.5g/dm3 platinum load. The only differences between the combined reactor system and the single platinum and oxide catalysts were connected with the reactors volume which in the case of the single reactors was two times higher than the volume of the corresponding blocks of the combined system. During the tests the ammonia concentration in the engine exhaust gases at the inlet of the reactors was set to 400 ppm. The article contains the results of the physical and chemical active surface structure tests of the reactors with their active surface chemical microanalysis and its topographic pictures performed and taken with the Scanning Electron Microscope. The results obtained from the tests of the influence of the reactor type on the NOX and NO conversion and the content of NO2 in NOX are presented in this article in the form of the function of their operating temperature. Additionally, the results of measured ammonia slip at the outlet of the reactors are presented. The obtained results have shown that the usage of the combined oxide-platinum reactor allows for widening the SCR system effective operating temperature range with a low ammonia slip at its outlet. This was achieved by use of the platinum reactor block which features a high nitric oxides conversion efficiency at the operating temperatures which are lower than those of the oxide catalyst and which can also provide the high ammonia spices conversion rangeto lower the ammonia slip at system outlet.
Źródło:
Journal of KONES; 2012, 19, 3; 195-202
1231-4005
2354-0133
Pojawia się w:
Journal of KONES
Dostawca treści:
Biblioteka Nauki
Artykuł
Tytuł:
Examination of the ammonia dose influence on nitric oxides transformations into combined oxide - platinum SCR catalyst
Autorzy:
Kamela, W.
Kruczyński, S.
Powiązania:
https://bibliotekanauki.pl/articles/241805.pdf
Data publikacji:
2012
Wydawca:
Instytut Techniczny Wojsk Lotniczych
Tematy:
combustion engines
catalytic reactors
selective reduction
nitric oxides
air pollution
Opis:
This paper presents the test results obtained from the combined oxide-platinum catalytic reactor used in the NH3-SCR system. The first reactor block was extracted from the oxide catalyst used in trucks. As the second module of the reactor a block with platinum acting as a catalyst was used with 2.5g/dm3 platinum load. During the tests the ammonia concentrations in the engine exhaust gases at the inlet of the reactor system were set to 240, 320 and 400 ppm. The article contains the results of the physical and chemical active surface structure tests of both reactor blocks with their active surface chemical microanalysis and its topographic pictures performed and taken with the Scanning Electron Microscope. The results of the NOX and NO conversion and the content of NO2 in NOX are presented in this paper as the function of combined reactors system operating temperature with three different ammonia concentrations in the exhaust gases. Additionally, the results of the measured ammonia slip at the outlet of the combined reactor were presented. The obtained results have shown that the increase in ammonia dose at the inlet of the system increases the nitric oxides conversion with the minimum influence on the ammonia slip. By using the platinum based catalyst block it was possible to widen the whole reactor system effective operating temperature due to the high nitric oxides conversion efficiency of the platinum block achieved at low operating temperatures. A low ammonia slip at the outlet of the combined catalytic reactor was obtained by use of the platinum reactor block whose properties allow for the high ammonia conversion.
Źródło:
Journal of KONES; 2012, 19, 4; 253-258
1231-4005
2354-0133
Pojawia się w:
Journal of KONES
Dostawca treści:
Biblioteka Nauki
Artykuł
Tytuł:
Możliwości przemysłowego wykorzystania ditlenku węgla - badania nad zastosowaniem CO2 w procesie otrzymywania gazu syntezowego
Possibilities of carbon dioxide industrial utilization- research on CO2 application in synthesis gas production
Autorzy:
Więcław-Solny, L.
Łabojko, G.
Babiński, P.
Powiązania:
https://bibliotekanauki.pl/articles/282849.pdf
Data publikacji:
2009
Wydawca:
Polska Akademia Nauk. Instytut Gospodarki Surowcami Mineralnymi i Energią PAN
Tematy:
redukcja emisja CO2
gaz syntezowy
reforming parą wodną
autotermiczny reforming
reforming metanu ditlenkiem węgla
katalizatory tlenkowe zol-żel
reduction of CO2 emission
synthesis gas
steam reforming
autothermal reforming
carbon dioxide reforming of methane
sol-gel oxide catalyst
Opis:
Konieczność obniżania emisji ditlenku węgla z sektora energetycznego - zgodnie z polityką klimatyczną UE - wymagać będzie w najbliższych latach wskazania metod jego utylizacji lub zagospodarowania. O ile metody wydzielania ditlenku węgla wydają się znane i opanowane (wymagają jednak dostosowania skali przerobu takich instalacji), to metody jego dalszego zagospodarowania otwierają ścieżkę poszukiwań dla wielu ośrodków badawczych. W przypadku krajowych uwarunkowań geologicznych i zagospodarowania terenu, składowanie wydzielonego ditlenku węgla może być problematyczne. Wynika stąd potrzeba zaproponowania konkretnych rozwiązań jego przemysłowego zastosowania. W artykule dokonano przeglądu możliwych zastosowań ditlenku węgla (przemysł chemiczny, spożywczy). Dokonano charakterystyki katalizatora zol-żel, stosowanego w badaniach reformingu metanu ditlenkiem węgla. Prezentacja wyników badań suchego reformingu gazu ziemnego ditlenkiem węgla obejmuje wyniki uzyskane dla dwóch katalizatorów niklowych: przemysłowego (INS Puławy - katalizator G-0117-7H) i otrzymanego metodą zol-żel. Określono współczynniki konwersji, uzyskane w procesie suchego reformingu w reaktorze przepływowym dla różnych stosunków substratów na wejściu CO2/CH4. Omówiono podstawowe problemy procesowe, związane z zastosowaniem ditlenku węgla w procesie reformingu metanu - tworzenie depozytów węglowych.
The European Union has steadily strengthened and multiplied its actions to achieving maximum CO2 emission reduction from the energy sector. A wide range of separation and capture of CO2 from gas streams technologies currently exist. Carbon capture and storage is one of the potential method of controlling greenhouse gas emissions, but to solve the CO2 emission problem we need to develop new industrial CO2 recycle method. So, this paper focused on possibilities of CO2 industrial utilization. Recently, carbon dioxide reforming of methane becomes more attractive way to utilize carbon dioxide. It has been demonstrated that carbon dioxide reforming of methane produces synthesis gas (H2/CO =1), which is useful for the synthesis of acetic acid, dimethyl ether, hydrocarbons and oxo-alcohols. Carbon deposition over catalysts surface is the main problem for carbon dioxide reforming with methane. Therefore, the better activity and stability of catalysts are necessary to be improved. In this work, the carbon dioxide reforming of methane on commercial (INS Puławy G-0117-7H) and new sol-gel Ni-based catalyst was investigated. The carbon dioxide reforming of methane operated under molar ratio of CH4:CO2 = 1:1; 1:2; 2;1 at two different temperatures, 600 and 700?C. Results of the carbon dioxide reforming of methane showed activity with promising low carbonaceous deposition. The methane conversion increased with temperature growth, the molar ratio of obtained synthesis H2/CO was about 1 for CH4:CO2 = 1:1.
Źródło:
Polityka Energetyczna; 2009, T. 12, z. 2/2; 633-643
1429-6675
Pojawia się w:
Polityka Energetyczna
Dostawca treści:
Biblioteka Nauki
Artykuł
Tytuł:
Oil Recovery from Oilfield Produced Water Using Zinc Oxide Nano Particle as Catalyst in Batch and Continuous System
Autorzy:
Alkhazraji, Hussein Ali Jabbar
Alatabe, Mohammed Jaafar Ali
Powiązania:
https://bibliotekanauki.pl/articles/1955502.pdf
Data publikacji:
2021
Wydawca:
Polskie Towarzystwo Inżynierii Ekologicznej
Tematy:
photocatalytic
produced water
oil content
advanced oxidation processes
AOPs
ZnO/UV
Opis:
This article describes the design of photo catalyst reactor for oil removing from produced water. Real produced water containing a combination of organic compounds was treated with zinc oxide nanoparticles. In this study, ultraviolet radiations were used to find the efficiency of removing the oil content from the water produced that brought from the Al-Ahdab oilfield in kut/ Iraq by advanced oxidation process (AOP) using (ZnO/UV) in batch system and continuous system. In batch system were studied the effect of zinc oxide concentration (nanoparticles), time of irradiation, and pH. The highest removal rate of oil from the produced water (100%) was obtained during the following optimal conditions: ZnO NPs as catalyst = 55 mg/L, pH =3, at the time of irradiation of 90 minutes in batch experiments. In the continuous system, the effects of flowrate, number of UV-A lamp and time of reaction were studied, the results obtained were the efficiency of decomposition decreases with increasing the flow rate of solution in reactor, the maximum removal efficiency of the process (ZnO/UV) was 80% at 20 mL/min and irradiation time 120 min. In general, zinc oxide is beneficial through its high oil adsorption capacity in addition, It lowers the amount of oil in the produced water.
Źródło:
Journal of Ecological Engineering; 2021, 22, 8; 278-286
2299-8993
Pojawia się w:
Journal of Ecological Engineering
Dostawca treści:
Biblioteka Nauki
Artykuł
Tytuł:
Aluminum Oxide Formation On Fecral Catalyst Support By Electro-Chemical Coating
Powstawanie tlenku glinu na nośniku katalizatora FeCrAl przez osadzanie elektrochemiczne
Autorzy:
Yang, H. S.
Jang, D. H.
Lee, K. J.
Powiązania:
https://bibliotekanauki.pl/articles/355942.pdf
Data publikacji:
2015
Wydawca:
Polska Akademia Nauk. Czytelnia Czasopism PAN
Tematy:
FeCrAl
catalyst support
aluminum oxide formation
PEO
plasma electrolytic oxidation
electrochemical coating
nośnik katalizatora
tlenek glinu
plazmowe utlenianie elektrolityczne
elektrochemiczne osadzanie
Opis:
FeCrAl is comprised essentially of Fe, Cr, Al and generally considered as metallic substrates for catalyst support because of its advantage in the high-temperature corrosion resistance, high mechanical strength, and ductility. Oxidation film and its adhesion on FeCrAl surface with aluminum are important for catalyst life. Therefore various appropriate surface treatments such as thermal oxidation, Sol, PVD, CVD has studied. In this research, PEO (plasma electrolytic oxidation) process was applied to form the aluminum oxide on FeCrAl surface, and the formed oxide particle according to process conditions such as electric energy and oxidation time were investigated. Microstructure and aluminum oxide particle on FeCrAl surface after PEO process was observed by FE-SEM and EDS with element mapping analysis. The study presents possibility of aluminum oxide formation by electro-chemical coating process without any pretreatment of FeCrAl.
Źródło:
Archives of Metallurgy and Materials; 2015, 60, 2B; 1503-1506
1733-3490
Pojawia się w:
Archives of Metallurgy and Materials
Dostawca treści:
Biblioteka Nauki
Artykuł
Tytuł:
Dobór nośnika tlenkowego dla katalizatora do niskotemperaturowego rozkładu N2O
The selection of oxide support of the catalyst for N2O emission abatement
Autorzy:
Inger, M.
Antoniak-Jurak, K.
Ruszak, M.
Kowalik, P.
Wilk, M.
Powiązania:
https://bibliotekanauki.pl/articles/1219506.pdf
Data publikacji:
2016
Wydawca:
Stowarzyszenie Inżynierów i Techników Przemysłu Chemicznego. Zakład Wydawniczy CHEMPRESS-SITPChem
Tematy:
nośnik katalizatora
rozkład N2O
gaz cieplarniany
catalyst support
N2O decomposition
greenhouse gas
Opis:
Badano przydatność nośników tlenkowych o zróżnicowanym składzie, do osadzania domieszkowanego spinelu kobaltowego jako fazy aktywnej katalizatora do redukcji emisji N2O. Określono wpływ temperatury kalcynacji na porowatość, wielkość porów i ich rozkład, nasiąkliwość wodną oraz wytrzymałość mechaniczną kształtek nośnika. Ze względu na bardzo wysoką wytrzymałość mechaniczną i korzystną strukturę porowatą (wysoki udział makroporów), najlepsze właściwości, spośród badanych nośników, w aspekcie preparatyki katalizatora do redukcji emisji N2O ma tlenek glinu uformowany metodą wytłaczania, kalcynowany w 1400°C.
The usefulness of oxide supports of a different chemical composition, for the deposition of multicomponent cobalt spinel catalyst as an active phase, designed for the reduction of N2O emission, was investigated. The influence of the calcination temperature on the porosity, pore size and its distribution, water absorbability and mechanical strength of the shaped support was determined. It was found that, due to the very high mechanical strength and beneficial porous structure (large contribution of macropores) the best properties, among the investigated supports, in terms of preparation of supported catalyst for N2O decomposition, has alumina oxide, formed by an extrusion method and calcined at the temperature of 1400°C.
Źródło:
Chemik; 2016, 70, 5; 255-260
0009-2886
Pojawia się w:
Chemik
Dostawca treści:
Biblioteka Nauki
Artykuł
Tytuł:
The activity of fused-iron catalyst doped with lithium oxide for ammonia synthesis
Autorzy:
Jedrzejewski, R.
Lendzion-Bieluń, Z.
Arabczyk, W.
Powiązania:
https://bibliotekanauki.pl/articles/779518.pdf
Data publikacji:
2016
Wydawca:
Zachodniopomorski Uniwersytet Technologiczny w Szczecinie. Wydawnictwo Uczelniane ZUT w Szczecinie
Tematy:
iron catalyst
ammonia synthesis
lithium oxide
Opis:
The iron catalyst precursor promoted with Al2O3, CaO, and Li2O was obtained applying the fusing method. Lithium oxide forms two phases in this iron catalyst: a chemical compound with iron oxide (Li2Fe3O4) and a solid solution with magnetite. The catalyst promoted with lithium oxide was not fully reduced at 773 K, while the catalyst containing potassium was easily reducible at the same conditions. After reduction at 873 K the activity of the catalyst promoted with lithium oxide was 41% higher per surface than the activity of the catalyst promoted with potassium oxide. The concentration of free active sites on the surface of the catalyst containing lithium oxide after full reduction was greater than the concentration of free active sites on the surface of the catalyst promoted with potassium oxide.
Źródło:
Polish Journal of Chemical Technology; 2016, 18, 2; 78-83
1509-8117
1899-4741
Pojawia się w:
Polish Journal of Chemical Technology
Dostawca treści:
Biblioteka Nauki
Artykuł
Tytuł:
Characterization of FeCo based catalyst for ammonia decomposition. The effect of potassium oxide
Autorzy:
Lendzion-Bieluń, Zofia
Pelka, Rafał
Czekajło, Łukasz
Powiązania:
https://bibliotekanauki.pl/articles/778513.pdf
Data publikacji:
2014
Wydawca:
Zachodniopomorski Uniwersytet Technologiczny w Szczecinie. Wydawnictwo Uczelniane ZUT w Szczecinie
Tematy:
ammonia decomposition
hydrogen
FeCo catalyst
Opis:
FeCo fused catalyst was obtained by fusing iron and cobalt oxides with an addition of calcium, aluminium, and potassium oxides (CaO, Al2O3, K2O). An additional amount of potassium oxide was inserted by wet impregnation. Chemical composition of the prepared catalysts was determined with an aid of the XRF method. On the basis of XRD analysis it was found that cobalt was built into the structure of magnetite and solid solution of CoFe2O4 was formed. An increase in potassium content develops surface area of the reduced form of the catalyst, number of adsorption sites for hydrogen, and the ammonia decomposition rate. The nitriding process of the catalyst slows down the ammonia decomposition.
Źródło:
Polish Journal of Chemical Technology; 2014, 16, 4; 111-116
1509-8117
1899-4741
Pojawia się w:
Polish Journal of Chemical Technology
Dostawca treści:
Biblioteka Nauki
Artykuł

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