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Total combustion

Transition metal oxides represent a prominent class of partial oxidation catalysts [1-3]. Nevertheless, materials belonging to this class are also active in catalytic combustion. Total oxidation processes for environmental protection are mostly carried out industriaUy on the much more expensive noble metal-based catalysts [4]. Total oxidation is directly related to partial oxidation, athough opposes to it. Thus, investigations on the mechanism of catalytic combustion by transition metal oxides can be useful both to avoid it in partial oxidation and to develop new cheaper materials for catalytic combustion processes. However, although some aspects of the selective oxidation mechanisms appear to be rather established, like the involvement of lattice catalyst oxygen (nucleophilic oxygen) in Mars-van Krevelen type redox cycles [5], others are still uncompletely clarified. Even less is known on the mechanism of total oxidation over transition metal oxides [1-4,6]. [Pg.483]

Due to oil combustion Due to gas combustion Due to coal combustion Total emission 2010 2025 G... [Pg.82]

Winnett, W.K. and M.P. Murphy. 1994. A novel sample introduction technique for combustion total organic carbon analysis in aqueous materials. Talanta 41 1627-1630. [Pg.234]

Combustible. Total Pressuie, mm Oxygen per cent, by Volume m Residual Atmosphere. [Pg.104]

In the industrial combustion sector, for a total French market of 6 Mt in 1993, the distribution between the four product types was as follows f/o ... [Pg.235]

Practically, one measures the quantity of total sulfur (in all its forms) contained in crude oil by analyzing the quantity of SO2 formed by the combustion of a sample of crude, and the result is taken into account when evaluating the crude oil price. When they are present, elementary sulfur and dissolved H2S can also be analyzed. [Pg.322]

Ash content EN 7 (M07-045) ISO 6245 ASTM D 482 Weight of residue from total combustion... [Pg.446]

Total sulfur NF EN 24260 ISO 4260 ASTM D 2785 Combustion in Wickbold burner and analysis... [Pg.450]

Total sulfur NF M 07-025 ASTM D 1552 Combustion at high temperature (induction furnace) and analysis... [Pg.450]

Total sulfur M 07-052 Combustion in furnace and colorimetric analysis... [Pg.450]

If there are hydrocarbons present in the formation that is being drilled, they will show in the cuttings as oil stains, and in the mud as traces of oil or gas. The gas in the mud is continuously monitored by means of a gas detector. This is often a relatively simple device detecting the total combustible gas content. The detector can be supplemented by a gas chromatograph, which analyses the composition of the gas. [Pg.27]

The easiest principle to appreciate is conservation of mass. Except for nuclear reactions, an element s total mass at the end of a reaction must be the same as that present at the beginning of the reaction thus, an element serves as the most fundamental reaction unit. Consider, for example, the combustion of butane to produce CO2 and H2O, for which the unbalanced reaction is... [Pg.22]

Environmental considerations also were reflected in coal production and consumption statistics, including regional production patterns and economic sector utilization characteristics. Average coal sulfur content, as produced, declined from 2.3% in 1973 to 1.6% in 1980 and 1.3% in 1990. Coal ash content declined similarly, from 13.1% in 1973 to 11.1% in 1980 and 9.9% in 1990. These numbers clearly reflect a trend toward utilization of coal that produces less SO2 and less flyash to capture. Emissions from coal in the 1990s were 14 x 10 t /yr of SO2 and 450 x 10 t /yr of particulates generated by coal combustion at electric utiUties. The total coal combustion emissions from all sources were only slightly higher than the emissions from electric utiUty coal utilization (6). [Pg.4]

Year Petroleum Gas-fired Internal combustion andgas turbine Total... [Pg.5]

Where T)is flame temperature in K MC is moisture content of the waste, expressed on a total weight basis SR is defined as stoichiometric ratio or moles O2 avadable/moles O2 required for complete oxidation of the carbon, hydrogen, and sulfur in the fuel, ie, 1/SR = equivalence ratio and is temperature of the combustion air, expressed in K. In Fnglish units, this equation is as follows ... [Pg.57]

Given the mechanisms and temperatures, waste combustion systems typically employ higher percentages of excess air, and typically also have lower cross-sectional and volumetric heat release rates than those associated with fossil fuels. Representative combustion conditions are shown in Table 11 for wet wood waste with 50—60% moisture total basis, municipal soHd waste, and RDF. [Pg.58]

Products of Incomplete Combustion Emission Limits. Products of iacomplete combustion typically are not directly measured duting the trial bum. Instead, levels of carbon monoxide (qv) emissions are used as an iadication of combustion efficiency. High combustion efficiencies are assumed to result ia acceptable levels of products of incomplete combustion. If carbon monoxide emissions are measured at less than 100 ppmv dry basis, the standard is met. However, if emissions are greater than 100 ppmv, no more than 20 ppmv of total hydrocarbons (qv) are allowed at the iaciaerator stack duting the trial bum. [Pg.45]

Elame-spread and smoke-density values, and the less often reported fuel-contributed semiquantitive results of the ASTM E84 test and the limited oxygen index (LOI) laboratory test, are more often used to compare fire performance of ceUular plastics. AH building codes requite that ceUular plastics be protected by inner or outer sheathings or be housed in systems aH with a specified minimum total fire resistance. Absolute incombustibHity cannot be attained in practice and often is not requited. The system approach to protecting the more combustible materials affords adequate safety in the buildings by aHowing the occupant sufficient time to evacuate before combustion of the protected ceUular plastic. [Pg.336]

The higher, long-chain dimers as weH as the tetramer dehydroacetic acid are far more stable and can be handled safely. The alkylketene dimers (AKDs) are shipped to the paper industry in tank tmcks in the form of ready-to-use aqueous emulsions with a total soHds content of 12—25% and a guaranteed shelf life of 30 days, as they have good hydrolytic stabHity. In this form they are not combustible Hquids, and are Hsted in the Canadian Domestic Substances List. [Pg.479]

Rates of production of lignite have continued to increase since 1960. In 1980 374 x 10 tons of coal equivalent (tee) were produced. One tee is the amount of energy available from combustion of a metric ton of coal having a heat content of 29.3 GJ, ie, 29.3 MJ/kg (12, 600 Btu/lb) (3). In 1989 this figure had risen to 460 x 10 tee. This 23% increase is somewhat less than the 28% increase in hard coal production during this period (see Coal). In 1990 the 1130 X 10 metric tons of lignite produced worldwide represented 24% of the total coal production. [Pg.153]

Detergents are metal salts of organic acids used primarily in crankcase lubricants. Alkylbenzenesulfonic acids, alkylphenols, sulfur- and methjiene-coupled alkyl phenols, carboxyUc acids, and alkylphosphonic acids are commonly used as their calcium, sodium, and magnesium salts. Calcium sulfonates, overbased with excess calcium hydroxide or calcium carbonate to neutralize acidic combustion and oxidation products, constitute 65% of the total detergent market. These are followed by calcium phenates at 31% (22). [Pg.242]


See other pages where Total combustion is mentioned: [Pg.239]    [Pg.468]    [Pg.318]    [Pg.412]    [Pg.4260]    [Pg.263]    [Pg.12]    [Pg.239]    [Pg.468]    [Pg.318]    [Pg.412]    [Pg.4260]    [Pg.263]    [Pg.12]    [Pg.187]    [Pg.451]    [Pg.799]    [Pg.480]    [Pg.481]    [Pg.24]    [Pg.29]    [Pg.389]    [Pg.33]    [Pg.494]    [Pg.4]    [Pg.10]    [Pg.28]    [Pg.39]    [Pg.40]    [Pg.40]    [Pg.45]    [Pg.191]    [Pg.194]    [Pg.459]    [Pg.480]    [Pg.426]   
See also in sourсe #XX -- [ Pg.27 ]




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