Big Chemical Encyclopedia

Chemical substances, components, reactions, process design ...

Articles Figures Tables About

Evolution rates, experimental determination

Experimental determination of Ay for a reaction requires the rate constant k to be determined at different pressures, k is obtained as a fit parameter by the reproduction of the experimental kinetic data with a suitable model. The data are the concentration of the reactants or of the products, or any other coordinate representing their concentration, as a function of time. The choice of a kinetic model for a solid-state chemical reaction is not trivial because many steps, having comparable rates, may be involved in making the kinetic law the superposition of the kinetics of all the different, and often unknown, processes. The evolution of the reaction should be analyzed considering all the fundamental aspects of condensed phase reactions and, in particular, beside the strictly chemical transformations, also the diffusion (transport of matter to and from the reaction center) and the nucleation processes. [Pg.153]

The previous concepts may be illustrated with the experimental determination of the evolution of reaction rate, measured by DSC at T = 60°C, for the copolymerization of methyl methacrylate (MMA) with variable amounts of ethylene glycol dimethacrylate (EGDMA), a vinyl-divinyl system (Sun et al., 1997). The reaction was initiated with 2,5-dimethyl-2,5-bis(2-ethylhexanoyl)peroxy hexane. [Pg.165]

Figure 34 The steps involved in determining the depth of container wall penetration under Canadian nuclear waste disposal conditions using data obtained in an electrochemical galvanic coupling experiment. (A) Crevice propagation rate (R cc Ic) as a function of temperature (T) (B) RCc as a function of 02 concentration [02] (C) calculated evolution of container surface temperatures and vault 02 concentrations with time in the vault (D) flux of 02 (Jo2) to the container surface as a function of time (E) predicted evolution of Rcc up to the time of repassivation (i.e., at [02]p) (F) total extent of crevice corrosion damage expressed as the total amount of 02 consumed (Q) up to the time of repassivation (G) experimentally determined maximum depth of wall penetration (Pw) as a function of 02 consumed (Q) (H) predicted maximum value of Pw up to the time of repassivation (fP)-... Figure 34 The steps involved in determining the depth of container wall penetration under Canadian nuclear waste disposal conditions using data obtained in an electrochemical galvanic coupling experiment. (A) Crevice propagation rate (R cc Ic) as a function of temperature (T) (B) RCc as a function of 02 concentration [02] (C) calculated evolution of container surface temperatures and vault 02 concentrations with time in the vault (D) flux of 02 (Jo2) to the container surface as a function of time (E) predicted evolution of Rcc up to the time of repassivation (i.e., at [02]p) (F) total extent of crevice corrosion damage expressed as the total amount of 02 consumed (Q) up to the time of repassivation (G) experimentally determined maximum depth of wall penetration (Pw) as a function of 02 consumed (Q) (H) predicted maximum value of Pw up to the time of repassivation (fP)-...
The most fundamental experimental determinations in model studies of proton transfer at weakly basic carbon are of the rate and equilibrium constants for carbon deprotonation to form an unstable carbanion (Eq. (1.1)). These parameters define the kinetic and thermodynamic barriers to proton transfer (Eq. (1.2) for Fig. 1.1). They are of interest to enzymologists because they specify the difficulty of the problem that must be solved in the evolution of proteins which catalyze proton transfer with second-order rate constants kcat/ m of 10 "-10 s that are typically ob-... [Pg.949]

In these equations D represents the corresponding diffusion coefficients, and Q the permeate flow rate. The first term of each equation gives the radial dispersion and the second one corresponds to the radial convection. The authors [5.103] used in their model, a biological kinetic rate expression (cp), which was obtained by independent experiments and analysis of a batch reactor, and also made an effort to account for and correlate the permeate flow decrease with the amount of produced biomass. The simulation curves obtained matched well the experimental results in terms of permeate flow rate evolution and product concentration. One of the important aspects of the model is its ability to theoretically determine the biomass concentration profiles, and the relation between the permeate flow rate and the calculated biomass concentration in the annular volume (Fig. 5.24). Such information is important since the biomass evolution cannot be determined by any experimental methodology. [Pg.215]

Here Eg is the semiconductor band gap [eV] and Eq (+4.44 eV) is the energy of a free electron on the Hi redox scale. ° " Activities of photochemical water-splitting catalysts are usually assessed with the rates of evolved gases [moFh] per catalyst amount [g] under the specified irradiation conditions. From the measured evolution rate [Hi], the apparent QE = 2[Hi]// of the catalyst can be calculated using the known photon flux I [mol/s] incident on the reaction mixture (as determined by, e.g., ferrioxalate actinometry ). If available, this information is included with the experimental conditions in Table 1. The structures of selected semiconductors are shown in Figures 2-4. [Pg.2]

The overall rate of isothermal crystallization of PTT (semicrystalline polymer) can be monitored by thermal analysis through the evolution of heat of crystallization by DSC as depicted in Figure 10. The sample is isothermally crystallized at preselected crystallization temperature (T) until complete crystallization. Half time of crystallization for the polymer is estimated from the area of the exotherm at r = const, where it is the time taken for 50% of the crystallinity of the crystallizable component to develop. The rate of crystallization of PTT can be easily characterized by the experimentally determined reciprocal half time, (tg j) . ... [Pg.590]

The basic relationship for the experimental determination of first-order rate constants is the extent of reaction (E.R.)-time profile where E.R. is defined either as ([R]o — [R])/[R]o (decay of reactant concentration) or as [P]/[R]o (evolution of product concentration). With these definitions in mind, we see that the scale on both x and y axes in the two plots in Figure 1.1 are actually apparent E.R. if [A]o is unity. In spectrophotometric kinetic analysis concentrations are not measured and it is necessary to assume that absorbance... [Pg.4]

Chapter 2 focused on the evolution of a nuclear spin system without examining how it achieves thermal equilibrium with the lattice by energy exchange. The lattice consists of all degrees of freedom, except those of the nuclear spins, associated with molecular rotations and translations in physical systems such as liquid crystals. Spin-lattice relaxation describes how the system of nuclear spins evolves towards thermal equilibrium with the large heat reservoir, the lattice. The spin relaxation rates with which the nuclei arrive at their equilibrium magnetization may be experimentally determined. There is a well-defined connection between the relaxation rates and the dynamics of the lattice provided that the coupling interactions between the nuclear spin system and the lattice are known. Thus, nuclear spin relaxation may be used to study motional processes in molecular systems. [Pg.111]

Since the overall rate of any electrochemical process at a fixed current density is directly proportional to the electroactive area A, it is obviously important to calculate simple, area-related parameters. Unfortunately, determining A is not always straightforward, either by calculation or from experimental determinations, e.g. the active area of many porous electrodes (e.g. particulate-packed beds or foam materials) depends strongly on the flow conditions (e.g. flooded- or trickle-flow), the extent of gas evolution, the degree of solid product build-up on the electrode and the cell geometry (i.e. the potential distribution). [Pg.79]

The photolytic decomposition of sodium bromate (NaBrOj), both unirradiated and exposed to Co ° gamma irradiations prior to photolysis, has been studied. The experimental details are given in ( ). In these determinations the gas evolution rate is not determined directly. Actually the total gas pressure is determined as a function of time, and to determine the decomposition rate it is necessary to differentiate the pressure vs. time curves. The differentiation is done numerically on a computer. The first step in the differentiation is to make a least square fit to a polynomial (usually second degree) through a specified number of data points. For example, five data points could be used. The second step is to compute the derivative at the center point... [Pg.166]

There is a second relaxation process, called spin-spin (or transverse) relaxation, at a rate controlled by the spin-spin relaxation time T2. It governs the evolution of the xy magnetisation toward its equilibrium value, which is zero. In the fluid state with fast motion and extreme narrowing 7) and T2 are equal in the solid state with slow motion and full line broadening T2 becomes much shorter than 7). The so-called 180° pulse which inverts the spin population present immediately prior to the pulse is important for the accurate determination of T and the true T2 value. The spin-spin relaxation time calculated from the experimental line widths is called T2 the ideal NMR line shape is Lorentzian and its FWHH is controlled by T2. Unlike chemical shifts and spin-spin coupling constants, relaxation times are not directly related to molecular structure, but depend on molecular mobility. [Pg.327]

Another approach to the determination of surface kinetics in these systems has been to combine molecular beams in the 10 2-10 1 mbar pressure range with the use of the infrared chemiluminescence of the C02 formed during steady-state NO + CO reactions. This methodology has been used to follow the kinetics of the reaction over Pd(110) and Pd(l 11) surfaces [49], The activity of the NO + CO reaction on Pd(l 10) was determined to be much higher than on Pd(lll), as expected based on the UHV work discussed in previous sections but in contrast with result from experiments under higher pressures. On the basis of the experimental data on the dependence of the reaction rate on CO and NO pressures, the coverages of NO, CO, N, and O were calculated under various flux conditions. Note that this approach relied on the detection of the evolution of gas-phase... [Pg.77]


See other pages where Evolution rates, experimental determination is mentioned: [Pg.370]    [Pg.221]    [Pg.31]    [Pg.146]    [Pg.469]    [Pg.336]    [Pg.423]    [Pg.169]    [Pg.114]    [Pg.255]    [Pg.506]    [Pg.56]    [Pg.114]    [Pg.280]    [Pg.51]    [Pg.484]    [Pg.211]    [Pg.781]    [Pg.586]    [Pg.273]    [Pg.84]    [Pg.147]    [Pg.143]    [Pg.482]    [Pg.230]    [Pg.961]    [Pg.211]    [Pg.130]    [Pg.18]    [Pg.509]    [Pg.210]    [Pg.812]    [Pg.149]    [Pg.18]    [Pg.36]    [Pg.266]   
See also in sourсe #XX -- [ Pg.631 , Pg.632 , Pg.633 , Pg.634 , Pg.635 , Pg.636 , Pg.637 , Pg.638 , Pg.639 , Pg.640 , Pg.641 , Pg.642 , Pg.643 , Pg.644 , Pg.645 ]




SEARCH



Rates determination

© 2024 chempedia.info