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1.
In the citric acid-Mn2+–H2SO4–KBrO3 system a hysteresis phenomenon in the switching on and off of the oscillations has been observed. The possible bifurcation diagrams of the system are discussed.
-Mn+2–H2SO4–KBrO3 . .
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2.
Catalytic properties of V–Mo–O systems have been studied in acrolein oxidation. When catalysts are activated in reaction mixtures at 673 K, then a solid solution of molybdenum oxides in reduced vanadium oxides is formed, which is responsible for deep oxidation. Also, several compounds are produced, which by their activity and selectivity to acrylic acid formation are arranged in the sequences VMo3O11VMo2O8+x>V6Mo4O25, and VMo3O11>VMo2O8+xV6Mo4O25, respectively.
V–Mo–O . 673 K , , , : VMo3O11VMo2O8+x>V6Mo4O25, : VMo3O11>VMo2O8+xV6Mo4O25.
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3.
Reduction kinetics of NiO–MoO3 catalysts in H2 at 573–723 K has been studied. Reduction activation energies Ea have been determined. The degree of NiO–MoO3 reduction is shown to increase with increasing NiO content.
NiO–MoO3 H2 573–723 . E NiO–MoO3 . , NiO–MoO3 NiO .
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4.
Kinetic regularities of triphenylphosphite ozonide reaction with triphenylphosphite have been studied at T=–75°C to –40°C. The rate of ozonide consumption is estimated as W=k1[(C6H5O)3P·O3]+k2[(C6H5O)3P·O3][(C6H5O)3P], where k1=(2.03±0.39)×10–5s–1(–50°C), 1gk2=(3.82±0.33)–(6.61±0.32)/gq dm3/mol s and =2.303RT kcal/mol.
–75°C –40°C . : W=k1[(C6H5O)3P·O3]+k2[(C6H5O)3P·O3][(C6H5O)3P], k1=(2,03±0,39)·10–5–1(–50°C); 1g k2=(3,82±0,33)–(6,61±0,32)/ /·, =2,303·RT /
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5.
The decomposition of calcium carbonate fine powder in a flowing nitrogen atmosphere has been investigated by non-isothermal thermogravimetry at heating rates in the range, 10–50 deg min–1. The analog percentage weight change record was digitized at 1 deg intervals. The resulting data, transformed into dimensionless extents of reaction and calculated rates of reaction, was then subjected to the Arrhenius, Friedman and Generalized Kissinger analyses, using a recently developed FORTRAN program system. The value ofn namely 0.39 ±0.04, resulting when the data is analyzed assuming an nth order reaction, strongly indicates that the most probable rate controlling step is a three-dimensional diffusion process (D4 mechanism), withE=172.4 kJ·mol–1 andA=1.97·104 K–1·min–1. Reasons for the wide disparity in previously reported kinetic data are discussed.
Zusammenfassung Die Zersetzung von feinpulvrigem Calciumcarbonat im Stickstoffstrom wurde durch nicht-isotherme Thermogravimetrie bei Aufheizgeschwindigkeiten von 10–50 °C/min untersucht. Die analoge prozentuale Gewichtsverlustregistrierung wurde in Intervallen von einem Grad digitalisiert. Die erhaltenen, in solche eines dimensionslosen Reaktionsgradcs überführten Daten und berechnete Reaktionsgeschwindigkeiten wurden der Arrhenius-, der Friedmann- und einer verallgemeinerten Kissinger-Analyse unterzogen, wobei ein kürzlich aufgestelltes FORTRAN-Programm benutzt wurde. Der unter der Annahme einer Reaktion n-ter Ordnung fürn erhaltene Wert von 0.39 ±0.04 ist ein nachdrücklicher Hinweis darauf, daß der geschwindigkeitsbestimmende Schritt höchstwahrscheinlich ein dreidimensionaler Diffusionsprozeß (D4-Mechanismus) mitE=172.4 kJ·mol–1 undA=1.97·104 K–1·min–1 ist. Gründe für die weitreichende Verschiedenheit der bisher mitgeteilten kinetischen Daten werden diskutirt.

10–50° . , , 1. , , , , , . n- , =0,39 ±0,04 , , e (4 ) E=172, 4 · –1 =1,97·104 –1·–1. .


To be presented at the 14th North American Thermal Analysis Society Conference, San Francisco, CA, September 15–18, 1985.  相似文献   

6.
The thermal decomposition of anhydrous Ce(NO3)3 has been studied. The thermal decomposition reaction is described by the second order kinetic equation, [1/(1–)]–1=kt. The apparent activation energy was determined asE a=104 kJ mol–1 while the enthalpy of the reaction was estimated asH r=111.1 kJ mol–1. The decomposition reaction differs from that observed for Nd(NO3)3.
Zusammenfassung Die thermische Zersetzung von wasserfreiem Ce(NO3)3 wurde untersucht. Die thermische Zersetzung wird durch die Geschwindigkeitsgleichung zweiter Ordnung[1/(1–)]–1=kt, beschrieben. Für die scheinbare Aktivierungsenergie wurde ein Wert von 104 kJ mol–1 und für die Enthalpie der Reaktion ein Wert von 111,1 kJ mol–1 ermittelt. Die Zersetzungsreaktion unterscheidet sich von der für Nd(NO3)3.

. : [1/(1–)]– 1=kt. a, 104 · –1, H r, 111.1 · –1. .


The authors wish to thank the Council for Scientific and Industrial Research and the University of Pretoria for financial assistance.  相似文献   

7.
It is established that the hydrocarbon coverage (0<1) formed at T<400 K on the Ir surface is oxidized upon oxygen exposures to CO and H2O by an adsorption mechanism. Complete oxidation to CO2 and H2O is achieved at T350 K after C2H4 exposures of the oxygen coverage.
, (<1), T<400 K Ir, CO H2O . CO2 H2O T350 K C2H4 .
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8.
The effect of representing dielectric properties in terms of the complex polarizability c = – i is examined. Loss curves ( and tan ) are shifted towards higher frequencies, revealing the existence of new relaxations and allowing the clarifications of ones already known. We have calculated the shift ratios (at maximum or tan )/ (at maximum or tan ) from the more conventional empirical equations representing the dielectric behavior. Some examples are given.  相似文献   

9.
The pyrolysis of cyclohexyl allyl ether and thioether has been studied in a stirred-flow reactor in the temperature range of 360–470 °C and pressures up to 10 Torr. The first order rate coefficients yielded the Arrhenius parameters log A=11.22±0.23, Ea=169±3 kJ mol–1 and log A=10.42±0.12, Ea=140±3 kJ mol–1, respectively. The mechanism of the pyrolysis of alkyl allyl ethers, thioethers and amines is discussed using literature data.
360–470°C 10 . : log A=11,22±0,23, Ea=169±3 / log A=10,42±0,12, Ea=140±3 /, . , .
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10.
Singlet triplet intersystem crossing quantum yields were determined for n-butyraldehyde, using the photosensitized cis-trans isomerization of piperylene to monitor the process. At room temperature and 313 nm, 0.58±0.05 and 0.72±0.05 were obtained for the triplet yield in the vapor phase and in isooctane, respectively.
- - - . 0,58±0,05 0,72±0,05 313 .


For Part I, see Ref. /1/  相似文献   

11.
The gasification with steam of a bituminous coal from Peñarroya (Cordoba, Spain) (H—O) and of several samples prepared from either by acid treatment (H—H, H—N, H—F and H—F(3)) or by thermal treatment (H—O—C) was studied under both dynamic and isothermal conditions (10 deg/min and 40 min at 1000°).It was found that only for the samples prepared by hydrofluoric acid treatment, H-F and H—F(3), did the gasification effected under such experimental conditions take place in a complete manner.
Zusammenfassung Die Dampfvergasung von bituminöser Kohle (H—O) (Penarroya, Cordoba, Spanien) und von daraus durch Säurebehandlungen (H—H, H—N, H—F und H-F(3)) oder thermische Behandlung (H—O—C) hergestellten Proben wurde unter dynamischen und isothermen Bedingungen (10 °/min und 40 min bei 1000°) untersucht. Es wurde festgestellt, daß nur die durch Flußsäurebehandlung hergestellten Proben (H—F und H—F(3)) unter den experimentellen Bedingungen vollständig vergasbar sind.

(10°/ 40 1000°) () , . , , , .


The authors are grateful to the CAICYT of Spain for the financial support on Project No. 0794/82.  相似文献   

12.
It is a well known fact that when supported on different supports, a transition metal may show different catalytic behavior. In some cases it is claimed that the differences in the acidity of supports are due to this phenomenon. In this work, by adding increasing amounts of MgO to Al2O3, the number of acid sites and hence the acidity of Al2O3 were monotonically decreased. The behavior of Ru supported on these mixed supports was investigated with IR, and it is concluded that the interaction between metal and acid sites on the surface is the most important factor for the changing properties.
, , . . Al2O3 MgO Al2O3. Ru -, , -.
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13.
Approximate equation to calculate the effectiveness factor of catalyst for SO2 oxidation to SO3 has been derived. Calculated data agree well with those predicted by a quasi-homogeneous model.
. .
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14.
The cubic spinel Fe2MoO4 was studied in air by DTA, DTG, TG and X-ray in the temperature interval 298–1173 K. From these studies, it was concluded that above the Néel temperature Fe2MoO4 undergoes an irreversible crystalline phase transition from cubic to tetragonal at 623 K, wherec/a is 1.022. Above 723 K, surface oxidation followed by bulk oxidation of the spinel occurs. At 948 K, after about half the total weight gain due to oxidation, a compound is formed which was confirmed by X-ray as ferrimolybdite, Fe2O3·3–4 MoO3, indicating that in Fe2MoO4 the Mo4+ is more readily oxidized than the Fe2+. Above 940 K, further oxidation of Fe2+ and Mo4+ into their respective oxide occurs. About 13 % of the MoO3 vaporizes, and the rest melts at 1028 K.
Zusammenfassung Das kubische Spinell Fe2MoO4 wurde in Luft im Temperaturbereich von 298 bis 1173 K durch DTA, DTG, TG und Röntgen untersucht. Aus diesen Studien wurde gefolgert, daß oberhalb der Neel Temperature ein irreversibler kristalliner Phasenübergang des Fe2MoO4 aus der kubischen in die tetragonale Form bei 623 K stattfindet, wobeic/a=1.022 beträgt. Oberhalb von 725 K findet eine Oberflächenoxidierung des Spinels statt, der eine allgemeine Oxidation folgt. Bei 948 K, nachdem etwa die Hälfte der infolge der Oxidation auftretenden Gewichtszunahme erfolgte, wird eine durch Röntgen als Ferrimolybdit bestätigte Verbindung gebildet (Fe2O3·3–4 MoO3), welche zeigt, daß in Fe2MoO4 das Mo4+ leichter oxidiert wird als das Fe2+. Oberhalb von 940 K erfolgt eine weitere Oxidation von Fe2+ und Mo4+ zu ihren entsprechenden Oxiden. Etwa 13% des MoO3 verdampft und das übrige schmilzt bei 1028 K.

, , Fe2MoO4 298–1173 . , Fe2MoO4 623 , / 1.022. 723 , , . 948 Fe2O3. 3–43, . , Fe2MoO4 Mo4+ , Fe2+. 940 Fe2+ Mo4+ . 13% MoO3 , 1028 .


The author wishes to thank the Chemistry Division of BARC for helping with the high-temperature X-ray pattern.  相似文献   

15.
Zinc exchanged zeolite X was found to catalyze effectively the dehydrosulfurization of ethanethiol. The catalytic activity correlated linearly with the degree of ion exchange and increased with the reaction temperature. The role of zinc cations in the reaction examined is discussed and suggestions concerning the reaction mechanism are put forward.
X, Zn, . . .
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16.
Active sites for ethylene homologation (3C2H42C3H6) and ethylene metathesis (C2H412C2+C2H413C22C2H413C1) were discriminated by adding platinum to a reduced molybdena silica catalyst, and the former was presumed to be composed of several molybdenum species, while the latter was presumed to be composed of one molybdenum species.
(3C2H42C3H6) (C2H412C2+C2H413C22C2H413C1) . , , .
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17.
Redox properties of some isomers of tungstovanadophosphoric heteropoly anions have been studied. Rate constants of electron transfer from -1, 2, 3-PW9V 2 V VIVO 40 7– to PW11VVO 40 4– (k=1.1±0.2)×102 dm3/mol s) and from PW10VVVivO 40 6– to -1,2,3-PW9V 3 V O 40 6– (k=1.4±0.2)×102 dm3/mol s) have been measured in 30% CH3COOH at pH 3 and 20°C.
- . PW11VVO40 4– -1,2,3-PW9V 2 V VivO40 7– (k=(1,1±0,2)·102 3/·), -1,2,3-PW9V 3 V O40 6– PW10VvVivO40 6– (k=(1,4±0,2)·102 3/·) pH=3 30%- CH3COOH 20°C.
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18.
In DSC studies of liquid-quenched ternary chalcogenide glasses Te80Ge20–xA x V (AV=Sb, Bi), the characteristic temperatures (glass transition and crystallization temperatures) were determined. Changes in the thermal stabilities of these glasses, depending on the element A (Sb, Bi) from group V of the periodic table and on its content in the alloy were evaluated. Moreover, the effect of changes in the glass composition on the glass formation ability expressed by the parameter Kg1 was determined.
Zusammenfassung In DSC-Untersuchungen abgeschreckter ternärer Chalkogenidgläser des Typs Te80Ge20–xA x v (Ax=Sb, Bi) wurden die charakteristischen Temperaturen (die GlasÜbergangs- und Kristallisationstemperaturen) bestimmt. Die Änderungen der Thermostabilität dieser Gläser wurden in Abhängigkeit von dem Element A (=Sb, Bi) aus der V Gruppe der Periodensystems und von seinem Gehalt in der Legierung ausgewertet. Ausserdem wurde der Einfluß der Änderungen in der Glaszusammensetzung auf die Glasbildungsfähigkeit, ausgedrückt durch den Parameter Kg1, bestimmt.

Résumé On a déterminé par analyse calorimétrique différentielle (DSC) les températures caractéristiques (températures de transition vitreuse et de cristallisation), des verres ternaires à chalcogénures formés par trempe à partir du liquide, du type Te80Ge20–xA x v (Av=Sb, Bi). On a évalué la variation de la stabilité thermique de ces verres en fonction de l'élément A (=Sb, Bi) du Vème groupe du tableau périodique et de sa teneur dans l'alliage. De plus, on a déterminé l'effet des variations de la composition du verre sur la capacité de formation du verre qui s'exprime par le paramètreK g1.

Te80Ge20–xA x v (Av=Sb, Bi), , . A(=Sb,Bi) . , K gl, .


Research supported by the U. S. National Science Foundation under Grant No. GF 421 76  相似文献   

19.
A linear correlation between the logarithm of rate constant (2kt) for recombination of tertiary peroxy radicals (ROO)* and * constants of substituents R was found to be 1g 2kt=lg 2k t ° . The calculated values are 1g 2k t ° =4.59±0.08 and *=5.56±0.35.
I (2kt) (ROO) R: 1g 2kt=lg 2k t ° . , 1g 1g 2k t ° =4,59±0,08 =5,56±0,35
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20.
Molecular isotope exchange of CO with14CO for Rh6(CO)16/Sn(II)–SiO2, Rh6(CO)16/Al2O3, Rh(I)(CO)2/Al2O3, Rh4(CO)12/Al2O3 carbonyl complexes of rhodium has been studied. Estimates of the activation energies and a mechanism of the CO exchange are suggested.
, (Rh6(CO)16/Sn(II)–SiO2, Rh6(CO)16/Al2O3, RhI(CO)2/Al2O3, Rh4(CO)12/Al2O3), 14CO. CO .
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