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Total Oxidation of Methanol

KIT-6 aged at 100°C with the same composition synthesized by other methods (RG reactive grinding citrate synthesis using citrate complexes) [26]. [Pg.60]


Formaldehyde is produced by oxidation of methanol or oxidative dehydrogenation of methanol. Oxidation of methanol (route (a) in Topic 5.3.2] is a strongly exothermic reaction (AH = -243 kj mol ) that is carried out in a pressure-less oxidation with air in a multi-tubular reactor. The reaction is catalyzed by an iron/molybde-num oxide contact, with Fe2(Mo04) being the active catalytic species. The oxidation is carried out at 350 °C with quantitative methanol conversion. The main side reaction is the total oxidation of methanol to CO2 and water. [Pg.478]

Further interaction between Ru-OH and the partially oxidized organic molecule on the surface leads eventually to the total oxidation of methanol to CO2 and H2O. [Pg.112]

The direct anodic oxidation of methanol became much more attractive after it was shown that platinum-ruthenium alloys are catalytically much more active in this reaction than pure platinum (pure ruthenium is totally inactive in this reaction). [Pg.366]

Figure 4.10 shows temperature influence on the process results formaldehyde yield reaches its maximum (about 40%) with temperature raise to 520 °C and total methane conversion increase. Above 520 °C, CO and C02 are detected in reaction products. Their formation rates noticeably increase with temperature. The occurrence of these compounds in the system is explained by sequential formaldehyde transformation to intense degradation products in the high temperature range. After-oxidation of methanol synthesized in the system also contributes to formation of these products. [Pg.118]

Hence, the total number of coulombs produced in a year from 10,000 tons of methanol would be 3 x 108 x 6 x 105 C (since 1 F - 105 C). Thus the oxidation of methanol in a fuel cell (10,000 tons per year) would produce 1.8 x 1014 C. [Pg.331]

Let us suppose that the total current from all the fuel cells used in the electricitygenerating plant is I A. The number of seconds in a year is 3.1 x 107 and (as It is coulombs since t is the time in seconds), / = 3.1 x 107 = 1.8 x 1014 or 1 = 6.6 x 106 A. Now, all this current would be converted to electrical energy in the fuel cells at (say) about 0.7 V, which is a reasonable potential in the oxidation of methanol in a fuel cell with a good electrocatalyst. Hence, we should produce 4 x 106 W or about 4000 kW. [Pg.331]

At steady state, Equations 6.48 and 6.49 are equal to zero, and the total current of methanol oxidation is expressed as... [Pg.333]

Manganese oxides have long been known to be catalysts for a variety of gas clean-up reactions. Manganese/copper mbced oxide (Hopcalite) is the catalytically active component in gas mask filters for CO CO is converted to CO2 at room temperature [4]. Further applications of manganese oxide catalysts are the NH3 oxidation to N2 [5], the combustion of VOC [6,7] and methane [8], the oxidation of methanol [7], the O3 decomposition [9] and the NOx reduction [14]. Perovskite-type oxide catalysts (e.g. LaMnOs) have been proven to be effective catalysts for the total oxidation of chlorinated hydrocarbons [10]. Several studies have shown that besides preparation method and calcination temperature the kind... [Pg.489]

The oxidation of methanol starts below 300° C. in the presence of a catalyst and quantities ranging up to 60 per cent of the total amount used in any experiment are decomposed. Not far from the oxidation temperature of the alcohol, formaldehyde undergoes decomposition into carbon monoxide and hydrogen. As much as 50 per cent of the formaldehyde which is formed may decompose in this way under certain conditions and ill the presence of certain catalysts. The oxidation of hydrogen to water... [Pg.140]

A test case is the investigation of selective oxidation of methanol to formaldehyde over metallic copper. This process occurring as dehydrogenation and/or oxydehydrogenation was studied extensively by in-situ NEXAFS and earlier by surface science. These studies brought about the relevance of unique oxygen species termed as sub oxide ° for the selective catalytic reaction. Conventional copper oxides were identified to catalyse the total oxidation and bare metal was found to be inactive. A target for in-situ XPS was thus the search for a sub oxide, the confirmation of its relevance for selective oxidation and the... [Pg.115]

As seen from these data, the loading of parent NaY zeolite with iron oxide via trinuclear Fe carbonyl as a precursor increases greatly the total rate of methanol conversion because of the appearance of oxidative active centers. In contrast, the use of carbonyl complexes of four and more nuclearity resulted in a dramatic drop of MeOH conversion even in comparison to the starting material. It should be noted that all Fe-containing samples have the same amount of iron oxide (about 1 wt %, metal basis), and such an effect can be explained only on assuming the formation of multilayer oxide deposits that cover the outer zeolite surface including its pore mouths. This assumption was verified by measuring the surface area for this set of samples that decreases from about 700 mVg for NaY down to a few tens m /g for three last samples in Table 5. [Pg.109]

The total electrochemical oxidation of methanol, involving 6 electrons, can be represented by ... [Pg.105]

The synthesis of formaldehyde from selective oxidation of methanol over a thin layer of electrolytic silver catalyst is a well-known industrial process that occurs in the temperature range of 850-923 K at atmospheric pressure. Since the total reaction is highly exothermic and fast, requiring very short contact time (0.01 s or less), the use of a silicon MSR was demonstrated to improve conversion up to 75% and 90% selectivity at safe conditions within the flammability limits [29]. [Pg.781]


See other pages where Total Oxidation of Methanol is mentioned: [Pg.111]    [Pg.1090]    [Pg.59]    [Pg.59]    [Pg.59]    [Pg.785]    [Pg.788]    [Pg.111]    [Pg.1090]    [Pg.59]    [Pg.59]    [Pg.59]    [Pg.785]    [Pg.788]    [Pg.187]    [Pg.366]    [Pg.135]    [Pg.55]    [Pg.198]    [Pg.213]    [Pg.213]    [Pg.354]    [Pg.363]    [Pg.77]    [Pg.45]    [Pg.95]    [Pg.248]    [Pg.169]    [Pg.554]    [Pg.215]    [Pg.218]    [Pg.183]    [Pg.117]    [Pg.176]    [Pg.139]    [Pg.146]    [Pg.857]    [Pg.320]    [Pg.282]    [Pg.281]    [Pg.2034]    [Pg.88]    [Pg.304]   


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