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Manganese oxide pressure

Initially Mn was discovered to lower the methane selectivity and increase the olefin selectivity. More specifically, it was reported by Kolbel and Tillmetz that more than 50% Mn the remainder being Fe or by Bussemeir et about equal parts of Fe and Mn led to these beneficial F-T effects. In contrast to these results, van Dijk et did not find any changes in the product formation when adding manganese oxide to an Fe F-T catalyst, although this work had been performed at atmospheric pressures, whereas the work of Kolbel and Tillmetz and Bussemeier was done at conditions close to industrial ones. [Pg.32]

Marble is formed from carbonate sediments, the most common of which is limestone. It is composed mostly of calcite. Pure marble is white, but it is easily stained by impurities such as iron oxide (red or brown) or manganese oxide (black). When the grains of calcite in limestone are exposed to heat and pressure, the mineral recrystallizes, forming a dense mass of inter-grown crystals. This makes marble stronger and slightly more dense than its parent rock. [Pg.48]

With adjustment of the steam/methane ratio, the reactor can produce a synthesis gas with CO/H2 = 1/2, the stoichiometric proportions needed for methanol production. This mixture at approximately 200 atm pressure is fed to the methanol unit where the reaction then proceeds at 350°C. Per pass conversions range from 30 to 50 over the catalyst— typically a supported copper oxide with a zinc, chromium, or manganese oxide promoter 3... [Pg.926]

Consider the reaction 3Mn203(s) == 2Mn304(s) + (l/2)02(g). Utilizing the data tabulated below, estimate the temperature at which the equilibrium pressure of 02(g) over the two manganese oxide phases is 0.20 atm. State any assumptions that you make. [Pg.259]

In addition to the estimated properties, we measured the thermochemistry of several important vapor species. These measurements were conducted in a Knudsen effusion cell using special line-of-sight vaporization under subambient pressures with flowing O2 and H2O vapor mixtures [4]. The gaseous species over silica [5], manganese oxide [6], lanthana, alumina, and palladium metal were detected and relative partial pressures measured as a function of temperature. These vapor pressure measurements were calibrated by using the known metal atom or binary metal oxide volatility as a calibration source. Oxide species concentrations were measured relative to that of a reference compound, e.g., metal atom. The identification of oxide and hydroxide compounds was facilitated by Ae technique of threshold electron ionization [7]. These data were then evaluated using estimated entropy functions and the third law temperatures. [Pg.602]

Example Problem The adsorption of N2 gas onto a sample of dry manganese oxide, weighing 0,3144 g, was measured volumetrically at three partial pressures of the N2 gas 0.098, 0.196, and 0.294. The volumes adsorbed at these pressures were 1.550, 1.904, and 2.22 ml, respectively, measured under ambient conditions of 22"C and 747 mm Hg of atmospheric pressure. Calculate the specific surface area of this mineral in units of square meters per gram. [Pg.351]

Even the simple ammoniiun chromates can undergo thermal decomposition [4, 6, 7, 12] which yields very active Cr (III) oxides on decomposition in the air. Partial formation of higher chromium oxides is observed at reduced pressures [6]. Since these decomposition reactions release a considerable quantity of heat, they must be carried out in thin layers (flat dishes) the mildest conditions are obtained if only one spot in the dish is heated at a time and that spot is pushed onto a cold surface as soon as the material starts to react. The thermal decomposition of NH4,Mn04 in air leads to explosions vacuiun decomposition yields, apart from NH4NO3, manganese oxides [Mn (III)-Mn (IV)], which are pseudo-morphous to the starting crystals [2]. [Pg.1673]

Lazier. Lazier (6) invented and assigned to the DuPont Company the next catalyst to be described. This was covered by a patent issued in 1931 and the catalyst, itself, was zinc oxide, manganese oxide, and chromium oxide. Depending on the manganese ratio and operating conditions (350-475 C and 267-900 atm. pressure) this catalyst could produce 20 to 50% higher alcohols in addition to methanol. [Pg.360]

Iron oxide (Fej.yO) and iron manganese oxides (Fei. Mn ,)i.yO Mn H20-decomposition Temperature (673-1173 K) and atmospheric pressure Ehrensberger et al. (1995)... [Pg.217]


See other pages where Manganese oxide pressure is mentioned: [Pg.371]    [Pg.328]    [Pg.1100]    [Pg.99]    [Pg.445]    [Pg.710]    [Pg.218]    [Pg.117]    [Pg.735]    [Pg.328]    [Pg.312]    [Pg.257]    [Pg.55]    [Pg.35]    [Pg.419]    [Pg.2640]    [Pg.446]    [Pg.243]    [Pg.3143]    [Pg.17]    [Pg.280]    [Pg.602]    [Pg.655]    [Pg.528]    [Pg.420]    [Pg.395]    [Pg.603]    [Pg.776]    [Pg.778]    [Pg.555]    [Pg.2639]    [Pg.479]    [Pg.360]    [Pg.333]    [Pg.335]    [Pg.333]    [Pg.335]    [Pg.152]    [Pg.99]    [Pg.514]   
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Manganese oxidation

Manganese-oxidizing

Oxidants manganese

Oxidation Pressure

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