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Oxidant, supply

If stored for too long, magnesium oxide can convert to magnesium carbonate or hydroxide with resultant loss of activity as an acid acceptor. Magnesium oxide supplied in stick form overcomes this problem. Some forms of pelletised magnesium oxides can be too hard to break down in soft compounds and problems can arise from hard undispersed ceramic -like particles. [Pg.131]

In ideal combustion 0.45 kgs (1 lb.) of air combines with 1.8 kgs (4 lbs.) of oxygen to produce 1.2 kgs (2.75 lbs.) of carbon dioxide and 1.02 kgs (2.25 lbs.) of water vapor. Carbon monoxide, carbon dioxide, nitrogen and water vapor are the typical exhaust gases of ordinary combustion processes. If other materials are present they will also contribute to the exhaust gases forming other compounds, which in some cases can be highly toxic. Imperfect combustion will occur during accidental fires and explosion incidents. This mainly due to turbulence, lack of adequate oxidizer supplies and other factors that produce free carbon (i.e., smoke) particles, carbon monoxide, etc. [Pg.45]

An important problem in research on NO formation in the combustion of coal and other nitrogen-containing fuels is to find the amounts of oxides supplied by atmospheric nitrogen and by nitrogen in the fuel. H. Semerjian and A. Vranos12 consider that in the latter case the governing role belongs to the reactions... [Pg.410]

Zhang J etal., 2001, Fuel Cell (Methanol) Sensor with Small Load Resistance and High Oxidant Supply. WO 01/35478. [Pg.184]

Considering the oxidant supply to the surface, it has been shown that there is an oxidant gas concentration Emit below which no heterogeneous ignition can take place. [Pg.179]

Having now determined to total amount of nuclear electricity required, the thorium fuel input to the energy amplifiers can be calculated from the design data of Rubbia and Rubio (1996). The thermal output from the prototype design reactor is 1500 MW, with a fuel amount of 27.6 t in the reactor (Fig. 5.42). The fuel will sit in the reactor heat-generating unit for 5 years, after which the "spent" fuel will be reprocessed to allow for manufacture of a new fuel load with only 2.9 t of fresh thorium oxide supply. This means that 2.6/5 t y of thorium fuel is required for delivery of 5 x 1500 MWy of thermal power over 5 years, or 675 MWy of electric power, of which the 75 MWy is used for powering the accelerator and other in-plant loads. The bottom line is that 1 kg of thorium fuel produces very close to 1 MWy of electric power, and 1 kt thorium produces close to 1 TWh. ... [Pg.300]

CFA is omnipresent in pelagic sediments, ferromanganese nodules, and seamount crusts, and marine phosphorites on continental margins and seamounts. Supply of phosphate by oxidation of organic matter and pre-concentration of phosphate by iron oxyhy dr oxides, supply of calcium by dissolution of carbonates or carbonates acting as substrates, and supply of fluorine from seawater are all important factors in the formation of marine phosphorites. [Pg.3497]

Reducing flame. Should the oxidant supplied to a flame be insufficient to completely oxidize the fuel gas, oxygen will be taken from any available source. The blackening of lead glass in a reducing flame is the most appropriate example. Neutral flame. When the oxidant and fuel supplied to the flame are such that combustion is complete and neither is in excess, the flame is said to be neutral. [Pg.20]

B. After an overnight fast, fatty acids, released from adipose tissue, serve as fuel for other tissues. Carnitine is required to transport the fatty acids into mitochondria for P-oxidation. In the liver, P-oxidation supplies acetyl CoA for ketone body (acetoacetate and 3-hydroxybutyrate) synthesis. In a carnitine deficiency, blood levels of fatty acids will be elevated and ketone bodies will be low. Consequently, the body will use more glucose, so glucose levels will be decreased. [Pg.227]

Despite its brilliant results, it seems unlikely that the Solutia process can become a major source of phenol. Nitrous oxide availability is quite limited and its production on-purpose (by the conventional ammonium nitrate decomposition, which enables nitrous oxide of high purity to be produced for medical anesthetic applications, or even by selective oxidation of ammonia) would result too expensive. Therefore, the only reasonable scenario to exploit the Solutia process is its implementation close to adipic acid plants, where nitrous oxide is co-produced by the nitric oxidation of cyclohexanol-cyclohexanone mixtures and where it could be used to produce phenol instead of being disposed of However, the stoichiometry of the process is such that a relatively small phenol plant would require a world-scale adipic acid plant for its nitrous oxide supply. In fact, a pilot plant has been operated using this technology, but its commercialization has been postponed. [Pg.516]

A further requirement to be satisfied by the oxidant supply device is represented by dynamic performance in a wide range of air flow rates. This aspect is crucial in some hybrid power train operative modes characterized by high stack dynamics (full power or soft hybrid configurations, see Sect. 5.5). [Pg.111]

The results shown in previous sections suggest the crucial role of the oxidant supply system, in particular the effect of the stoichiometric ratio (air flow rate) on FCS efficiency and dynamic performance. In order to give further information about this issue, in this paragraph different air management strategies are closely examined, with particular reference to their influence on cell voltage uniformity and air compressor parasitic losses. [Pg.223]

Microfabrication processes have been used successfully to form micro-fuel cells on silicon wafers. Aspects of the design, materials, and forming of a micro-fabricated methanol fuel cell have been presented. The processes yielded reproducible, controlled structures that performed well for liquid feed, direct methanol/Oj saturated solution (1.4 mW cm ) and direct methanol/H O systems (8 mA cm" ). In addition to optimizing micro-fuel cell operating performance, there are many system-level issues to be considered when developing a complete micro power system. These issues include electro-deposition procedure, catalyst loading, channel depth, oxidants supply, and system integration. The micro-fabrication processes that have... [Pg.33]

Both gas chromatography and infrared analysis aire dependent upon the instrumentation being calibrated against certifled ethylene oxide supplies. Gas chromatography results are obtained as mol 9c, values which must then be converted to Specifications defined in mg/L. Infrared results are directly correlated to mg/L. [Pg.138]

P-Oxidation supplies NADH and FAD(2H), which are used by the electron transport chain for oxidative phosphorylation. As ATP levels increase, less NADH is oxidized, and the NADH/NAD ratio is increased. (4) Oxaloacetate is converted into malate because of the high NADH levels, and the malate enters the cytoplasm for gluconeogenesis,. (5) Acetyl CoA is diverted from the TCA cycle into ketogenesis, in part because of low oxaloacetate levels, which reduces the rate of the citrate synthase reaction. [Pg.436]

Cyclohexene oxide supplied by Fluka Chemicals, 99% purity. [Pg.485]

The synthetic utility of (i )-enoate 392 is illustrated in the stereoselective synthesis of the bengamide E derivative 399 (Scheme 88). Silyl protection of 392, reduction with DIBAL, and Sharpless epoxidation of the resulting allylic alcohol furnishes epoxy alcohol 396 as a 95 5 anti syn mixture. Conversion of the primary hydroxyl group of 396 to an iodide under neutral conditions followed by a metallation-elimination and subsequent in situ methylation provides the ether 397. Ozonolysis, desilylation with aqueous acetic acid, and a Dess-Martin oxidation supplies the a,jS-dialkoxy aldehyde 398. This, utilizing stannane Se addition, is then converted to 399 [135]. [Pg.378]

In this case the oxidant supply subsystem becomes similar to the fuel subsystem, as oxygen is also fed from a tank to the stack and needs to be recycled to evacuate the product water from the stack. [Pg.353]


See other pages where Oxidant, supply is mentioned: [Pg.426]    [Pg.428]    [Pg.435]    [Pg.670]    [Pg.232]    [Pg.409]    [Pg.81]    [Pg.294]    [Pg.431]    [Pg.431]    [Pg.304]    [Pg.113]    [Pg.57]    [Pg.356]    [Pg.177]    [Pg.180]    [Pg.9]    [Pg.882]    [Pg.501]    [Pg.3493]    [Pg.2511]    [Pg.2540]    [Pg.64]    [Pg.30]    [Pg.177]    [Pg.180]    [Pg.527]    [Pg.287]    [Pg.386]    [Pg.7]    [Pg.773]   
See also in sourсe #XX -- [ Pg.420 ]




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