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1.
The thermal desorption of atomic oxygen during the transformations BiO2 – x -Bi2O3 -Bi2O3is shown to be due to the removal of overstoichiometric oxygen from the bulk of -Bi2O3. Oxygen formed at the first stage is desorbed in a molecular form. The maximum desorption rate of atomic oxygen is found before the phase transformation -Bi2O3 -Bi2O3. The activation energy of the diffusion of excess oxygen in the -Bi2O3lattice is 30 kcal/mol.  相似文献   

2.
The interaction of the catalyst 5.16 wt % Pt/-Al2O3 with 4, 2, 2, and 4 + 2 pulses is studied using a setup involving the differential scanning calorimeter DSC–111 and a system for chromatographic analysis. Comparison of the results obtained with analogous data on Ni/Al2O3 and Co/Al2O3 suggests that methane activation occurs via a common pathway via dissociative chemisorption on the metal surface with the formation of 2 and carbon on all the catalysts studied. Carbon dioxide activation on Pt/Al2O3 differs from its activation on Ni()/Al2O3. It follows from the enthalpy of formation that carbon on Pt/Al2O3 is graphite-like in contrast to carbide carbon on Ni(Co)/Al2O3. This graphite carbon is more stable and less reactive.  相似文献   

3.
A V2O5/Al2O3 mixed solids sample was prepared with a molar ratio of 0.41 Na2O (4 and 10 mol%) was added in the form of sodium nitrate prior to calcination in air in the temperature range 500–1000C. Solid-solid interactions between V2O5 and Al2O3 were studied using DTA and TG curves and their derivatives together with XRD techniques.The results obtained showed that Na2O interacted with V2O5 at temperatures starting from 500C to yield a sodium/vanadium compound, Na0.3V2O5 which remained stable and decomposed in part by heating at 1000C. V2O5 exists in orthorhombic and monoclinic forms in the case of pure mixed solids and those containing 4 mol% of Na2O and preheated at 500C, and in monoclinic form in the case of the mixed solid doped with 10 mol% of Na2O.Heating of pure and doped mixed oxide solids at 650C resulted in the conversion of most of the V2O5 into AlVO4. Doping with sodium oxide enhanced the solid-solid interaction between V2O5 and Al2O3 at 650C to produce AlVO4. The produced AlVO4 decomposed completely on heating at 700C to form -Al2O3 and V2O5, (orthorhombic and monoclinic forms).The presence of Na2O was found to decrease the relative intensity of the diffraction lines of -Al2O3 (corundum) produced at 750C which indicated some kind of hindrance of the crystallization process.Heating of pure and doped mixed solids at 1000C resulted in a further crystallization of acorundum together with V2O5 and sodium vanadate, Na0.3V2O5. However, the intensities of diffraction lines relative to those of the sodium vanadium compound were found to decrease markedly by heating at 1000C, indicating partial thermal decomposition into vanadium and aluminium oxides.  相似文献   

4.
Kinetic regularities in the reaction of triphenyl phosphite ozonide with several thioacetals in CH2Cl2 solution at –15°C have been studied. The consumption rate of ozonides is described by the kinetic equation W=k0[(C6H5O)3P·O3]+k1[(C6H5O)3P·O3][R1R2C(SR3)2] Rate constants k0 and k1 for the thioacetals: (CH3H7S)2CH2, (C6H5S)2CH2, (C6H5CH2S)2CH, (n=C12H25–S)2CH2, (C3H7S)2C(H)CH3, (C3H7S)2C(H)C6H5, (C3H7S)2C(CH3)C6H5 and (C3H7S)2C(H)C10H9, increases with increasing the electron-donating power of subtituents Ri.
CH2Cl2 –15°C. : W=k0[(C6H5O)3P·O3]+k1[(C6H5O)3P·O3][R1R2C(SR3)2] k0 k1 (C3H7S)2CH2, (C6H5S)2CH2, (C6H5CH2S)2CH2, (n-C12H25S)2CH2, (C3H7S)2C(H)CH3, (C3H7S)2C(H)C6H5, (C3H7S)2C(CH3)C6H5, (C3H7S)2C(H)C10H9. .
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5.
When Eu2(SO3)3·3H2O is heated in air it forms after dehydration two sulfite-sulfate phases: Eu2(SO3)2SO2 and Eu2SO3(SO4)2. The latter phase is thermally remarkably stable and decomposes above 700°C via Eu2O2SO4 to Eu2O3. Anhydrous Eu2(SO3)3 and Eu2O2SO4 were also found as intermediates before Eu2O3 when the TG experiments were carried out in nitrogen but in other details the decomposition mechanism differs from that in air.
Zusammenfassung Eu2(SO3)3·3H2O bildet durch Erhitzen in Luft nach Dehydratation zwei Sulfit-Sulfat-Phasen: Eu2(SO3)2SO4 und Eu2SO3(SO4)2·Letztere ist thermisch bedeutend stabiler und zersetzt sich oberhalb 700°C über Eu2O2SO4 zu Eu2O3. Bei Durchführung der TG-Experimente in Stickstoff wurden als Zwischenprodukte vor Eu2O3 auch wasserfreies Eu2(SO3)3 und Eu2O2SO4 gefunden, in anderen Details weicht jedoch der Mechanismus der Zersetzung von dem der Zersetzung in Luft ab.

- Eu/SO3/2SO4 Eu2SO3/SO4/2. 700° Eu2O3 Eu2O2SO4. Eu2/SO3/3 Eu2O2SO4 , .


For Part VII, see ref. 6.  相似文献   

6.
Using DTA, TG and DTG methods, the reaction between RbNO3 and V2O5 in the molar ratio 65 in air atmosphere was studied. The reaction proceeds stepwise. In individual steps of the reaction the formation of RbV3O8, RbVO3 and Rb3V5O14 was observed. Rubidium pentavanadate is thermally unstable. At 1000°, RbVO3 and Rb2V4O11 were identified as products of its thermal decomposition. Rubidium tetravanadate was also prepared by the isothermal reaction of RbNO3 with V2O5 in the molar ratio 11.
Zusammenfassung Unter Anwendung der DTA-, TG- und DTG-Methoden wurde die Reaktion RbNO3-V2O6 bei dem Molverhältnis von 65 in Luft untersucht. Die Reaktion verläuft stufenweise. Bei den einzelnen Stufen der Reaktion wurde die Bildung von RbV3O8, RbVO3 und Rb3V5O14 beobachtet. Rubidiumpentavanadat ist thermisch instabil. Bei 1000° wurden RbVO3 und Rb2V4O11 als Produkte seiner thermischen Zersetzung beobachtet. Rubidiumtetravanadat wurde auch durch die isotherme Reaktion von RbNO3-V2O5 bei dem Molverhältnis von 11 hergestellt.

Résumé On a étudié par ATD, TG et TGD dans l'air, la réaction RbNO3-V2O5 (rapport molaire 65). La réaction s'effectue par étapes, avec formation de RbV3O8, RbVO3 et Rb3V5O14. Le pentavanadate de rubidium est thermiquement instable. A 1000°, RbVO3 et Rb2V4O11 ont été identifiés comme produits de la décomposition thermique. Le tétravanadate de rubidium a également été préparé par voie isotherme en faisant réagir RbNO3-V2O5 (rapport molaire 11).

, , RbNO3-V2O5 6 5. . RbV3O8, RbVO3 Rb3V5O14. 1000° RbVO3 Rb2V4O11, . RbVO3-V2O5 11.
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7.
Fine particle cobalt doped-Fe2O3 and Mn-Zn ferrites have been prepared by the thermal decomposition of N2H5Co x Fe1–x (N2H3COO)3.H2O wherex=1–10 atom% and (N2H5)3MnxZn1–x Fe2(N2H3COO)9· 3H2O wherex=0.2–0.8, respectively. Formation of these oxide materials has been confirmed by thermogravimetry and X-ray powder diffraction patterns. The fine particle nature of these oxide materials is evident from particle size analysis and surface area measurements.
Zusammenfassung Mit fein verteiltem Kobalt versetztes-Fe2O3 sowie Mn-Zn Ferrite wurden durch thermische Zersetzung von N2H5Co x Fe1–x (N2H3COO)3·H2O mit jc=1–10 Atomprozent bzw. (N2H5)3Mn x Zn1–x Fe2(N2H3COO)9·3H2O mitx=0,2–0,8 hergestellt. Die Bildung dieser Oxidstoffe wurde durch Thermogravimetrie und Pulverdiffraktionsmethoden bekräftigt. Die Feinkornstruktur dieser Oxidstoffe wird durch Korngrößenverteilungs- und Oberflächenmessungen augenscheinlich.

N2H5Co x Fe1–x (N2H3COO)3·H2O, x-1–10 %, (N2H5)3Mn x Zn1–x Fe2(N2H3COO)9 · 3H2O, x=0,2–0,8, , , -Fe2O3 Mn-Zn . . .
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8.
The effects of iron on the structural properties of Zn-borosilicate glass and Pb-metaphosphate glass were studied using X-ray diffraction,57Fe Mössbauer spectroscopy and IR spectroscopy. Zn-borosilicate glass was prepared with varying amounts of Fe2O3 (up to 30% wt.). It was found that the chemical form of added iron (-FeOOH, -Fe2O3 or Fe3O4) affects the Fe3+/Fe2+ ratio, as well as the distribution of iron ions at different coordination sites. At high concentration of iron the crystallization of zinc ferrite in the glass matrix takes place. X-ray diffraction and57Fe Mössbauer spectroscopy showed that the amount of zinc ferrite in Zn-borosilicate glass decreases with the following order of addition: -FeOOH-Fe2O3Fe3O4. In Pb-metaphosphate glass doped with high concentration of -Fe2O3, the crystallization of Fe3(PO4)2 is pronounced. The assignments of IR band positions and the corresponding interpretation are given. The importance of this study for the technology of vitrification of high-level radioactive wastes is emphasized.  相似文献   

9.
Diffuse reflectance spectra have been recorded for WO3/SiO2 and WO3/-Al2O3 catalysts after various steps of treatment of these samples, in particular, after treatment of WO3/SiO2 by HCl. It is shown that for WO3/-Al2O3 the temperatures of the onset of reaction and WO3 reduction coincide.
WO3/SiO2 WO3/-Al2O3 , , WO3/SiO2 HCl. , WO3/-Al2O3 .
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10.
3 % Ir/Al2O3 catalysts have been studied by means of temperature programmed reduction and oxidation. With growing degree of metal oxidation (higher Tox) reducibility of the catalysts at low temperatures decreases.
3% Ir/Al2O3 . ( ) .
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11.
The phase equilibria in the total range of component concentrations in the V2O5-Cr2O3 system up to 1000 °C were studied by means of phase powder diffraction and DTA. Two compounds exist in the system: CrVO4, melting incongruently at 860±5 °C, and Cr2V4O13, which decomposes in the solid state at 640±5 °C to CrVO4(s) and V2O5(s). At 645±5 °C, CrVO4 and V2O5 form a eutectic mixture with the CrVO4 content not exceeding 2% mol.
Zusammenfassung Mittels DTA und Pulverdiffraktionsaufnahmen wurde das Phasengleichgewicht des Systems V2O5-Cr2O3 bis 1000 °C im gesamten Konzentrationsbereich untersucht. Innerhalb des Systemes existieren zwei Verbindungen: CrVO4 mit einem inkongruentem Schmelzpunkt bei 860±5 °C und Cr2V4O13, das sich in festem Zustand bei 640±5 °C in CrVO4(s) und V2O5(s) zersetzt. Bei 645±5 °C bilden CrVO4 und V2O5 ein eutektisches Gemisch mit einem maximalen CrVO4-Gehalt von 2 mol%.

DTA V25-Cr23 1000° . : CrVO4, 860±5° Cr2V4O13, 640±5° CrVO4 V2O5, 645±5° CrVO4, 2 %.
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12.
Zusammenfassung Das Verbrennen von Mischungen der exothermen Systeme Al-NaF-NaNO3 und Al-CaF2-NaNO3 wurde durch Röntgenanalyse ergänzte DTA untersucht. Um den Einfluß des durch Dissoziation von NaNO3 gebildeten Sauerstoffs zu bestimmen wurden auch Mischungen, welche anstatt NaNO3 NaNO2 oder Na2O2 enthielten, geprüft.Zwei, bei 310° bzw. 850° einsetzende exotherme Reaktionen wurden in den Gemischen vom Typ Al-NaF-NaNO3 gefunden. Die erste ist der Dissoziation von NaNO3 zuzuschreiben, die zweite ist der Anwesenheit von Luft zuzuordnen.Beide exothermen Reaktionen wurden im System Al-CaF2-NaNO3 in Richtung höherer Temperaturen verschoben. Die Untersuchung der NaNO2- oder Na2O2-haltigen Gemische anstatt NaNO3 zeigte, daß die Dissoziation von NaNO3 den zum Verbrennen benötigten Sauerstoff liefert, andererseits würde letztere Reaktion sonst nur in begrenztem Ausmaß stattfinden.
Combustion of exothermic mixtures belonging to the system Al-NaF-NaNO3 and Al-CaF2-NaNO3 was investigated by DTA and X-ray analysis. In order to determine the influence of the oxygen generated by dissociation of NaNO3, the mixtures containing NaNO2 or Na2O2 instead of NaNO3 were also examined.Two exothermic reactions starting at 310° and 850° rsp. were found in the mixtures of the Al-NaF-NaNO3 type. The first is due to the dissociation of NaNO3 and the second proceeds independence of the availability of air.Both exothermic reactions were shifted to higher temperatures in the system Al-CaF2-NaNO3. Investigation of the mixtures containing NaNO2 or Na2O2 instead of NaNO3 has proved that the dissociation of NaNO3 supplies the oxygen required for combustion which should otherwise proceed only in a limited extent.

Résumé On a étudié, par ATD et par analyse aux rayons X, la combustion des mélanges exothermiques appartenant aux systèmes Al-NaF-NaNO3 et Al-CaF2-NaNO3. Afin de déterminer l'influence de l'oxygène engendré par la dissociation de NaNO3, on a étudié de même des mélanges contenant NaNO2 ou Na2O2 au lieu de NaNO3.On a trouvé, dans les mélanges du type Al-NaF-NaNO3, des réactions exothermiques à partir des temperatures respectives de 310° et 850°. La première est due à la dissociation de NaNO3 et la seconde dépend de l'air disponible.Dans le système Al-CaF2-NaNO3 les deux réactions sont déplacées vers les températures plus élevées. L'examen de mélanges contenant NaNO2 ou Na2O2 au lieu de NaNO3 à montré que c'est la dissociation de NaNO3 qui fournit l'oxygène nécessaire pour la combustion. Celleci n'aurait lieu, autrement, que d'une manière limitée.

, l-NaF-NaNO3 Al-CaF2-NaNO3. , NaNO3, , NaNO3, , NaNO2 Na2. , Al-NaF-NaNO3 , 310° 850°. , . Al-CaF2-NaNO3 . , NaNO2 Na2O2, , , , , .
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13.
A thermodynamic study is presented for the simultaneous synthesis of C1–C4 alcohols from synthesis gas. The equilibrium composition was calculated for the gaseous mixture containing Co, H2, CH3OH, C2H5OH, C3H7OH, n-C4H9OH and H2O. Operating industrial conditions were specifically considered.
C1–C4 -. , CO, H2, CH3OH, C2H5OH, C3H7OH, -C4H9OH H2O. .
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14.
The ammoxidation of 3- and 4-picolines has been studied over V2O5–SnO2/–Al2O3 catalysts prepared by surface impregnation technique. Best results were obtained for the generation of cyanopyridines in the temperature range 400–450°C and sub-stoichiometric value with respect to O2. Catalysts that were calcined above 700°C showed no activity.
3- 4- V2O5–SnO2/–Al2O3, . 400–450°C O2. , 700 K, .
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15.
ESR data for X(CuO) V2O5·8.3 MoO3 system heated at 400–550 °C indicate the occurrence of a copper state with dZ 2-ground state. Copper ions are orbitally ordered apparently in –Cu2+–O–Cu1+–O–Cu2+-chains.
B X(CuO) V2O5·8,3 MoO3 , 400–550°C dZ 2- . , , –Cu2+–O–Cu1+–O–Cu2+-.
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16.
Only H2S consumption and H2O formation was found in the sulfurization of CoMoK/Al2O3 water gas shift catalyst with H2S/H2, but CO2 was formed first, then CH4, H2O and H2S appeared in the later part of TPS with CS2/H2. Carbon deposition on the catalyst during the sulfurization with CS2/H2 caused a lower activity than the catalyst sulfurized with H2S but could be removed in the run of WGS reaction.
, CoMoK/Al2O3, H2S/H2 H2S H2O, CS2/H2 CO2 CH4, H2O H2S. CS2/H2 H2S, , .
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17.
m-Xylene conversion was studied over dealuminated Y type zeolites in hydrogen forms, SiO2 to Al2O3 ratios were varied from 4.86 to 12.95.
- . SiO2/Al2O3 4,86 12,95.
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18.
By IR spectroscopy and TPD the effect of vanadium content on the relative proportion of strongly acidic sites of V2O5/Al2O3 catalyst was studied.
- - V2O5/Al2O3.
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19.
The kinetics of isothermal-isobaric dehydration of Li5P3O10·5H2O in vacuum (p=10–1 hPa) and in water vapour atmosphere ( =23·hPa) was investigated by TG in the temperature range 40–140°. It was shown that the initial non-degradation removal of 1/10 of the crystal water, the rate of which is sensitive to , proceeds according to the laws of reversible topochemical reactions. In the next, irreversible degradation stage, where the bulk of the crystal water is removed, the kinetic characteristics of the process and the DSC effects exhibit a low sensitivity to the water vapour pressure. The peculiarities of Li5P3O10·5H2O dehydration were considered in comparison with the thermal behaviour of Na5P3O10·6H2O and K5P3O10·4H2O.
Zusammenfassung Die Kinetik der isotherm-isobaren Dehydratisierung von Li5P3O10·5H2O in Vakuum (p=10–4 hPa) und in Wasserdampfatmosphäre ( =23 hPa) wurde durch TG im Temperaturbereich von 40–140° untersucht. Es wurde gezeigt, daß die anfängliche, noch keine Zersetzung zur Folge habende Eliminierung von 1/10 des Kristallwassers, deren Geschwindigkeit von abhängt, nach den Gesetzen der reversiblen topochemischen Reaktionen abläuft. Im nächsten irreversiblen Zersetzungsschritt, in dem die Hauptmenge des Kristallwassers austritt, sind die kinetischen Kennwerte des Prozesses und die DSC-Effekte nur wenig vom Wasserdampfdruck abhängig. Die Besonderheiten der Dehydratisierung von Li5P3O10·5H2O werden im Vergleich mit dem thermischen Verhalten von Na5P3O10·6H2O und K5P3O10·4H2O erörtert.

40–140° - Li5P3O10 · 52 (=10–4 ) (=23 ). , 1/10 , . , - . L5310·52 Na5P3O10·6H2O K5310·42.
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20.
The surface properties of Pt-Dy/-Al2O3 catalysts have been investigated by TPR and HOT techniques. Catalytic properties in the reaction of n-hexane, cyclopentane, and benzene on Pt/-Al2O3 and Pt-Dy/-Al2O3 catalysts have been studied in a pulsed microcatalytic reactor. The effect of dysprosium in Pt-Dy/-Al2O3 catalysts is also discussed.
Pt-Dy/-Al2O3 TPR HOT. Pt/-Al2O3 Pt-Dy/-Al2O3 -, . Pt-Dy/-Al2O3.
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