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Extracting overall reaction

The basic idea of using TCR in a gas turbine is usually to extract more heat from the turbine exhaust gases rather than to reduce substantially the irreversibility of combustion through chemical recuperation of the fuel. One method of TCR involves an overall reaction between the fuel, say methane (CH4), and water vapour, usually produced in a heat recovery steam generator. The heat absorbed in the total process effectively increases... [Pg.141]

As the large-scale computational fluid dynamics (CFD) simulations often invoke simplifying the kinetics as one-step overall reaction, the extraction of such bulk flame parameter as overall activation energy is especially useful when the CFD calculation with detailed chemistry is not feasible. Based on the experimental results, the deduced overall achvation energies of the three equivalence ratios are shown in Figure 4.1.10a. It can be observed that the variation of with is nonmonotonic and peaks near the stoichiometric condition. [Pg.42]

The use of tetraoctylammonium salt as phase transfer reagent has been introduced by Brust [199] for the preparation of gold colloids in the size domain of 1-3 nm. This one-step method consists of a two-phase reduction coupled with ion extraction and self-assembly using mono-layers of alkane thiols. The two-phase redox reaction controls the growth of the metallic nuclei via the simultaneous attachment of self-assembled thiol monolayers on the growing clusters. The overall reaction is summarized in Equation (5). [Pg.28]

We first consider the simple example of an uncatalyzed Diels-Alder reaction shown in Scheme 50.2 in order to demonstrate the use of different excess experiments. The Diels-Alder reaction is known to exhibit second overall order kinetics, as shown in eq. (4). We demonstrate with this known case how reaction progress kinetic analysis may be used to extract the reaction orders in both substrate concentrations, [5] and [6]. ... [Pg.448]

Fig. 13.2. Results of the reaction path shown in Figure 13.1, plotted to allow the overall reaction to be extracted using the slopes-of-the-lines method. Fig. 13.2. Results of the reaction path shown in Figure 13.1, plotted to allow the overall reaction to be extracted using the slopes-of-the-lines method.
As an example, we consider the reaction path traced in the previous section (Fig. 13.1). To extract the overall reaction for each segment of the path, we construct a plot as described above. The result is shown in Figure 13.2. There are three segments in the reaction path the precipitation of kaolinite, the transformation of kaolinite to muscovite, and the continued formation of muscovite once the kaolinite is exhausted. There is a distinct overall reaction for each segment. [Pg.197]

Haifa Also called IMI. One of the two Wet Processes for producing phosphoric acid by the acidulation of phosphate rock the other is the Dorr process. The Haifa process uses hydrochloric acid for the acidulation and solvent extraction for the purification. It is economic only where by-product hydrochloric acid is available. The overall reaction is ... [Pg.121]

Patio [Spanish, a courtyard] A medieval process for extracting silver from argentite, Ag2S. The ore was mixed with salt, mercury, and roasted pyrites, which contains cupric sulfate. This mixture was crashed by stones dragged by mules walking on the paved floor of a courtyard. The overall reactions are ... [Pg.204]

Step 1 Write the equations representing the half-reactions as extracted from the overall reaction given and label as an oxidation and a reduction. [Pg.397]

Of the reaction steps, only the first three have values of AG° > 0 however, the large negative value of the fourth step makes the overall reaction AG°x negative, thus favoring the extraction of the complex. The first step can be measured by the determination of the dinitrato complex in the aqneons phase. The second is related to the distribution constant A btbp in the solvent system. Also, the formation constant of the aqneons U02(N03)2(TBP)2 can be measnred (for example by NMR on P of TBP in the aqneons phase). Thns, AG can be derived. [Pg.122]

A typical application of carrier-mediated transfer is the recovery of metal cations from aqueous phases. The overall reactions involved in the extraction and stripping stages can be represented by the following reversible reaction ... [Pg.655]

An estimate of the pK value for benzaldehyde radical-anion has also been obtained from fast cyclic voltammetry experiments over a range of pH values [14], Interpretation the results obtained in this case requires first deduction of an overall reaction scheme followed by numerical solution of the corresponding set of differential equations allowing simulation of the cyclic voltammogram. Reaction constants are then adjusted to give good simulations over a range of experimental conditions. The pKj can then be extracted from these reaction constants. [Pg.332]

Sodium dithionite (Na2S204) is a reductant that is commonly used for the extraction of Fe oxides from kaolin and from soils (both to determine the total amount of Fe oxides and to improve the dispersibility of the day minerals Mehra Jackson, 1960). The overall reaction may be written as ... [Pg.312]

After a long fallow period, other workers have recently begun to extend Challenger s arsenic biomethylation work (1-3). Cox and Alexander have studied this reaction by the mold Candida humicola (59-9/). The overall reaction may be summed up by the reaction shown in Eq. (6). Both cell extracts and whole cells of Methanobacterium strain M.o.H. converted arsenate to dimethylarsine (92). Investigations on C. humicola and other molds determined that the rate of (CH s production follows the growth rate pattern of the mold, and decreases when the mold reaches the resting phase (93). The methylated arsenic intermediates were identified by use of... [Pg.326]

The Purex process is used for almost all fuel reprocessing today. Irradiated UO2 fuel is dissolved in HNO3 with the uranium being oxidized to U02(N03)2 and the plutonium oxidized to Pu(NC>3)4. A solution of TBP in a high-boiling hydrocarbon, such as n-dodecane, is used to selectively extract the hexavalent U02(N03)2 and the tetravalent Pu(NC>3)4 from the other actinides and fission products in the aqueous phase. The overall reactions are... [Pg.481]

The side chain of such statins, the (3i ,5S)-dihydroxyhexanoates, is a key intermediate and are accessible by reduction of the diketo acids. One way is bioreduction with whole cells (Patel, 1993) with glycerol-grown suspensions of Adnetobacter calcoaceticus SC 13876, yields of 85% and 97% e.e. were achieved for the benzyloxy-(3P,5S)-derivative. If cell extracts were used and NAD+, glucose, and glucose dehydrogenase supplied, both intermediate monohydroxy (in the 3- and 5-position) compounds were produced before the desired dihydroxyhexanoate, and the overall reaction resulted in 72% yield and 98.5% e.e. (Patel, 2001). [Pg.394]

For chemical and physical processes across microdroplet/solution interfaces, obs having dimensions of s or dm mor s is often proportional to r " ( = 0, 1 or 2). A linear relationship between obs and has been reported for the extraction of a neutral compound such as ferrocene derivatives from water into a micro-oil-droplet without adsorption at the microdroplet/water interface [18,19] and for a photographic dye formation reaction in an oil-in-water emulsion [23]. The proportionality of a kobs versus r plot has been reported for a relatively slow process such as a photographic dye formation reaction [23,29,42], electron transfer [43-45] and adsorption at the micro-oil-droplet/water interface [19,20]. For the chemical reaction with the rate-determining step in a solution phase or a microdroplet in a microdroplet/solution system, fcobs is independent of r[23]. Based on the droplet size dependence of the reaction rate, the rate-determining step of the overall reaction processes across a microdroplet/solution interface is analysed and the reaction mechanism can be discussed in detail. [Pg.194]

The adsorption of reactant molecules at the interface significantly affects the overall reaction rate in the two-phase system by the catalytic function of the interface. The liquid-liquid interface itself is a unique catalyst with such a flexible adsorbed area, which can be expanded or shrunk easily only by stirring or shaking. The increase of the adsorbed reactant molecules results in the promotion of reaction rate and the product will be extracted into the organic phase depending on its hydrophobicity. [Pg.330]


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