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1.
A supported ruthenium catalyst on alumina prepared from Ru3(CO)12 has been studied by infrared and X-ray photoelectron spectroscopy (XPS). The triatomic cluster is retained on the support but breaks down at 150°C. Complete elimination of the carbonyl groups requires heating at 350°C under vacuum. XPS studies show that the decomposed catalyst does not change on further reduction in H2 at 400°C. The ruthenium atoms remain trapped within the pores of the support.
Al2O3, Ru3(CO)12, (XPS). , 150°C . 350°C . XPS , H2 400°C . .
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2.
The response signal in PSA measurements – the transition time – can be considerably amplified by using a special pulse technique which we call alternating pulse current (APC). The sensitivity of the method is thereby considerably increased. This is achieved by modulating the current with a high frequency in a square wave mode during the stripping phase in such a way, that cathodic and anodic pulses alternate, so that the species to be determined is stripped and – at least partially – redeposited during the procedure. The transition time is not affected by the absolute values of the currents and of the times they flow. The amplification is determined by their respective ratios only. The equations holding are derived and proven experimentally by measurements on very dilute Pb solutions. The APC-PSA technique has also been applied for systems termed irreversible such as U and Tc, where also a considerable amplification could be achieved. The probable reasons are discussed and future developments and investigations are depicted.  相似文献   

3.
Interaction of both satured and unsaturated hydrocarbons with tetrahedral Co2+ ion complexes lodged in the zeolite skeleton is reported on the basis of diffuse reflectance spectra. While saturated hydrocarbons do not affect the coordination sphere of the Co-complex, the unsaturated hydrocarbons change considerably the distortion of the tetrahedral Co-complex.
- Co2+ - . - Co-, - - Co-.
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4.
The oxidation of methane on supported chromia was studied at temperatures varying between 423 and 743 K and CH4/O2 ratios between 1 and 9 in a differential reactor. The main reaction products observed were carbon monoxide and formaldehyde. The rates of reaction obey a power law expression.
, 423 743 CH4/O2 1 9, . . .
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5.
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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6.
The initial rate of carbon formation during cyclopentane reaction has been studied on different Pt/Al2O3 catalysts of varying metal dispersity. It has been shown that coke deposition on the metal is a structure sensitive reaction which is preferably produced on large metallic particles. On the other hand, coke deposition on the whole catalyst is relevant to cyclopentadiene formation and is a structure insensitive reaction since the initial rate of coke deposition on the whole catalyst is proportional to the metallic surface area.
Pt/Al2O3 . , , . , , , .. .
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7.
Studies of SO2 oxidation on a molten component of vanadium catalysts in non-steadystate conditions indicates that the kinetics agree fairly well with an oxidation-reduction mechanism. In the low temperature range (<790 K) tetravalent vanadium can be partially crystallized.
. , - . ( 790 ) .
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8.
Catalysts with nonuniform distribution of the catalytically active component (Pt) over their porous support (Al2O3) have been studied. A nonuniform activity distribution changes not only the reaction rate but also the kinetics can be different on these catalysts.
(Pt) (Al2O3). , , .
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9.
Initial stage of the reaction of CCl4 with V2O5 has been studied by MS and XPS techniques. According to the proposed mechanism dissociatively chemisorbed CCl4 transforms to CO2 via adsorbed COCl2, while surface vanadium atoms involved are gaining step by step two chlorine atoms before the formation of the volatile end-product VOCl3.
CCl4 V2O5 . - CCl4 CO2 COCl2, VOCl3.
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10.
Investigations on the temperature-programmed reduction of 3% Ir–Fe/Al2O3 catalysts after their oxidation at different temperatures Tox have been carried out. A substantial promoting effect of iridium on the reducibility of iron has been observed for all the investigated catalysts, at Tox applied.
- 3% Ir–Fe/Al2O3 (Tox). Tox.
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11.
Kinetics of H2 evolution in the RhCl3–NaH2PO2–HCl–H2O system has been studied. As found by31P NMR, Rh(I) complexes with the Rh–P(OH)2O bond are formed and play the role of catalysts in the subsequent H2 evolution reaction.
H2 RhCl3–NaH2PO2–HCl–H2O. 31P Rh(I) Rh–P(OH)2O, H2.
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12.
Photoadsorption activity of SnO2 with respect to O2 and NO after CO chemisorption has been revealed to be drastically increased. Photoadsorption is suggested to be sensitized by surface carbonates formed due to CO chemisorption.
. , .
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13.
Simultaneous thermogravimetry (TG), derivative thermogravimetry (DTG), differential thermal analysis (DTA), and evolved gas analysis (EGA) by mass spectrometry (MS) have been used to determine the decomposition path for tetraamineplatinum(II) chloride and cis- and trans-diamineplatinum(II) chloride. Unequivocal identification of the evolved gases was done by direct insertion probe mass spectrometry.The thermal decomposition of (NH3)4PtCl2 occurred in two steps. The first was endothermic loss of two moles of ammonia producing a mixture of cis- and trans-diaamineplatinum(II) chloride. The second step was decomposition of the diamine complex to metallic Pt and N2, HCl, and NH4Cl. Reduction of Pt(II) to metallic Pt was coupled with oxidation of ammonia to molecular nitrogen and protons.
Zusammenfassung Simultane Thermogravimetrie (TG), derivative Thermogravimetrie (DTG), Differentialthermoanalyse (DTA) und Analyse der entwickelten Gase (EGA) durch Massenspektrometrie (MS) wurden zur Bestimmung des Reaktionsverlaufs bei Zersetzung von Tetraminplatin(II)-chlorid sowie cis- und trans-Diaminplatin(II)-chlorid herangezogen. Die eindeutige Identifizierung der entwickelten Gase erfolgte durch Massenspektrometrie mit direkter Probeneinführung. Die thermische Zersetzung von (NH3)4PtCl2 erfolgt in zwei Schritten. Der erste ist die endotherme Abspaltung von zwei Mol Ammoniak unter Bildung eines Gemisches von cis- und trans-Diamin-platin(II)-chlorid. Der zweite Schritt ist die Zersetzung des Diaminkomplexes zu metallischem Pt, H2, HCl und NH4Cl. Die Reduktion von Pt(II) zu metallischem Pt ist mit der Oxydation von Ammoniak zu molekularem Stickstoff und Protonen gekoppelt.

-, -, -, - - (II) - (II) . (II). -. (NH3)4PtCl2 . - -(NHN3)2PtCl2. , , . .


The technical assistance of G. J. Dechert is gratefully acknowledged.  相似文献   

14.
The effect of the support preparation technique (solgel and coprecipitation) on the final Pt/ZnAl2O4 catalyst is presented. The structural properties of the solids obtained are correlated to the selectivity and activity for isobutane dehydrogenation in H2 and He reaction media. If a highly dispersed catalyst is suitable, the support has to be prepared by the sol-gel method.
( — ) Pt/ZnAl2O4. H2 He. , — .
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15.
Systems V2O5–KHSO4 and V2O5–K2SO4 have been studied by the51V NMR method. The first system demonstrates the same states of vanadium as the previously studied V2O5–K2S2O7, in this system a compound with an equimolar ratio of components has been found. In V2O5–K2SO4 the state of vanadium differs from the above systems and the formation of a compound with V/K=4 is observed.
51V KHSO4–V2O5 K2SO4–V2O5. , K2S2O7–V2O5, . K2SO4–V2O5 V/K4.
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16.
Alumina-supported MoO3 and WO3 catalysts were activated for the metathesis of propene by thermal treatment in Ar. Temperatures up to 1140 K are required for catalysts with low metal contents. These exhibit the highest specific activities though they are known to be highly resistant to reduction. It is proposed that the active sites are formed from Mo(VI) and W(VI) species under the conditions employed.
MoO3 WO3, Al2O3, . 1140 . , , . , , Mo W.
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17.
MoO3/Al2O3 is reduced at least partly by sulfur which is formed from H2S in sulfidation with H2S/N2 mixture. SO2 formation during TPD of MoO3/Al2O3 with presorbed H2S provides evidence for the explanation.
MoO3/Al2O3 , H2S/N2. SO2 MoO3/Al2O3, H2S, .
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18.
Abstract A series of rare earth transition metal perovskites has been synthesized and the catalytic activity tested for 2-propanol decomposition. The effect of rare earth ions on the catalytic activity can been understood from the correlations obtained between the physico-chemical properties and the catalytic activity of the perovskites.
, , 2-. , - .
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19.
It is shown that, in contrast to classical impregnation methods, in bimetallic catalyst production the texture of the carrier is stabilized by introducing the promoting ion on the surface of Pt/Al2O3 with vapors of CrO2Cl2 or SnCl4. This is shown by a relatively slower decrease of the specific area and the volume of the pores upon calcination.
, Pt/Al2O3- CrO2Cl2 SnCl4 . .
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20.
The non-catalyzed oscillation reaction of the aniline-KBrO3–H2SO4 system has been followed potentiometrically. The concentration regions of the beginning of oscillation are given in a triangular diagram. Also studied was the dependence of the induction period on concentration of the participants, which was described by a kinetic equation. The oscillation region extends to lower KBrO3 concentrations, the number of the oscillation jumps increases, and the induction period is shortened with increasing acidity.
-KBrO3–H2SO4. . . KBrO3, .
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