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Reaction operator

Figure 4. TEM and HRTEM images of (a) 6.5 nm Co nanoparticles and (b) Co-core/Au-shell nanoparticles using Co nanoparticles as the seed material. Lattice distances measured by HRTEM as well-matched to known Au lattice parameters for the (111) plane (inset). The average size of the Co-core/Au-shell nanoparticles is ca. 6.4 nm, which is similar to the initial size of the Co nanoparticles because the atom exchange process is the only operative reaction. (Reprinted from Ref [145], 2005, with permission from American Chemical... Figure 4. TEM and HRTEM images of (a) 6.5 nm Co nanoparticles and (b) Co-core/Au-shell nanoparticles using Co nanoparticles as the seed material. Lattice distances measured by HRTEM as well-matched to known Au lattice parameters for the (111) plane (inset). The average size of the Co-core/Au-shell nanoparticles is ca. 6.4 nm, which is similar to the initial size of the Co nanoparticles because the atom exchange process is the only operative reaction. (Reprinted from Ref [145], 2005, with permission from American Chemical...
Whether the mixing is associated with other operations reaction, heat transfer. [Pg.468]

Under the conditions of operation, reaction I is first-order in species B and is characterized by a rate constant equal to 15 ksec-1. Reaction II is first-order in species C and is characterized by a rate constant equal to 3 ksec-1. A stream containing 2.0 kmoles/m3 of A and 0.5 kmoles/m3 of B is available at a rate of 0.75 m3/ksec. [Pg.347]

A combination of Co-mediated amino-carbonylation and a Pauson-Khand reaction was described by Pericas and colleagues [286], with the formation of five new bonds in a single operation. Reaction of l-chloro-2-phenylacetylene 6/4-34 and dicobalt octacarbonyl gave the two cobalt complexes 6/4-36 and 6/4-37 via 6/4-35, which were treated with an amine 6/4-38. The final products of this domino process are azadi- and azatriquinanes 6/4-40 with 6/4-39 as an intermediate, which can also be isolated and separately transformed into 6/4-40 (Scheme 6/4.11). [Pg.464]

TABLE 5.4. Recently described examples for aqueous-biphasically operated reactions... [Pg.119]

Figure 12.4 Some modes of operation of semicontinuous reactors (a) gas-liquid reaction (b) gas-solid (catalyst or reactant) reaction (c) cyclic operation (reaction)-) and regeneration)- -)) for deactivating catalyst... Figure 12.4 Some modes of operation of semicontinuous reactors (a) gas-liquid reaction (b) gas-solid (catalyst or reactant) reaction (c) cyclic operation (reaction)-) and regeneration)- -)) for deactivating catalyst...
While many researchers have used the 1,3-APT process to generate cyclic nitrones, it is clear that the operating reaction pathway in the oxime to isoxazolidine conversion may not always be predicted. In the work of Aurich and co-workers (317,318), the polycyclic isoxazohdine 292 was isolated as the major product from thermolysis of oxime 293 and may have been formed via two separate reaction paths (Scheme 1.61). In the proven route, initial 1,3-APT of 293 formed a 1,4-oxazine nitrone (294), which acted as the acceptor for the second 1,3-APT with the remaining oxime function. The cyclic nitrone 295 so formed underwent a 1,3-dipolar cycloaddition with the allyl ether forming the isolated polycyclic isoxazolidine adduct 292. [Pg.52]

In this paper we present a comparative study of the catalytic properties of bare Si02, 4% Mo03/Si02 and 5% V205/Si02 catalysts in the partial oxidation of methane to formaldehyde. The role of the acidic properties and reduced sites, evaluated in steady state conditions, is addressed. A co-operative reaction path-... [Pg.44]

Do CS plane defects occur under catalyst operating reaction conditions in oxides ... [Pg.43]

Rohan had suggested that the operative reaction in the development of chocolate aroma might be a Strecker degradation of the amino acid fraction. Bailey et al. (8) demonstrated quantitatively that three aldehydes, which could be related to leucine, valine, and alanine, were prominent in the volatiles from a typical sample of roasted, ground cacao beans. [Pg.305]

In the process industry, there are only four basic operations reaction, separation, mixing, and heat transfer. The traditional unit operation is to perform each task in one or more pieces of equipment sequentially, for example, heat transfer in heat exchangers and reaction in reactors. Combining two or more tasks in one piece... [Pg.132]

Const, (power) dissipation energy per unit vessel volume Const, impeller discharge flow energy Turbulent dispersion Gas-liquid operation Reaction requiring microscale mixing... [Pg.111]

Commercial success of an industrial catalytic process depends on the feedstock cost, number of process steps, operability, reaction conditions, etc. A successful industrial process must strike the right balance between the selectivity and activity of the catalyst on the one hand, and its price and life on the other. Also, society demands that the manufacturing processes of the twenty-first century are inherently safe and environmentally friendly. [Pg.37]

A valuable application of LC is to rapidly establish optimum chemical reaction conditions. After developing the separation, the first step is to collect and identify the individual reaction products. Most detectors have a linear response of peak height to amount present therefore, once the characteristic retention time and detector response versus concentration are known, it is easy to establish the optimum reaction conditions. In chromatography the retention time establishes the absence or presence for each compound of interest. The calibration curves indicate the amount of each component. Comparison of the chromatograms of reaction mixtures is a simple and rapid method of determining the preferred operating reaction conditions and concentrations. Since HPLC is much faster than TLC and is carried out in a closed system, a minor benefit is that it is easier to prevent oxidative degradation in HPLC than in TLC. [Pg.51]

In addition to chemicals, biological catalysts such as enzymes can be used to catalyze reactions in SC CO2. Since the first attempt to operate reactions in supercritical fluids published by Randolph et al. [34], various type of enzymes were studied lipase, oxidase, decarboxylase, dehydrogenase, proteinase, etc. [33,35-37]. The effect of different parameters was extensively reported by Ballesteros et al. [35]. Enzyme activity and stability in supercritical conditions as well as the benefits of using supercritical fluids for enzymatic reactions (improved reaction rates, control of selectivity, etc.) have been demonstrated [36]. [Pg.186]

This system demonstrates some of the complications which can arise in TBP extraction when acid adducts and metal complexes of similar stability arise, as with U02Cl2(TBP)2 and HC1-TBP(H20)3. Also the nature of the extractant species in the organic phase may vary with extractant concentration and for diluted TBP a hydration number of four (not six) was found for the TBP-HCl adduct. " If the homogeneous mechanisms were operative, reactions Such as those in equations (69) and (71) would occur wholly in the organic or the aqueous phase. In the latter case the U02Cl2(TBP)2 complex would then pass into the organic phase in a separate mass transfer step. Little information is available on which of these mechanistic possibilities applies in any particular U02 extraction system. [Pg.911]

The reaction of CCl with CO is reported to result in the formation of considerable quantities of phosgene [1824a], and it is interesting to speculate upon the carbon monoxide behaving as a thermodynamic sink for dichlorine in the well-known and industrially operated reaction [2165] ... [Pg.239]

We have witnessed a veritable Golden Age of asymmetric chemistry over the last 25-30 years, yet we need to be mindful of the fact that the scientific discipline is actually over a century old. For several decades fhe development was rather sluggish, but this has now been amply compensated for as new results and achievements are reported at high speed and in quantities that virtually make it impossible to stay abreast wifh aU aspects of the field. Nonetheless, the need for technologies that can convert a substrate molecule into a desired product in high chemical and optical yield is very pronounced - both from academia and in industry - and therefore the large investments made can easily be justified. To operate reactions under catalytic conditions is in demand (not forgetting fhat about 80% of all che-... [Pg.59]


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See also in sourсe #XX -- [ Pg.3 ]




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