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Theoretical consideration

Simple considerations of the electronic structure of carbenes indicate that, of the six valence electrons associated with the divalent carbon, four are taken up by the two covalent bonds and two are non-bonding. The divalent carbon atom has two orbitals available to accommodate [Pg.157]

Much of the interest in carbenes has centred on the existence of these low-lying states of different multiplicity. A great deal of effort has been devoted to attempts to deduce the populated states of carbenes of various compositions, their energies and associated molecular dimensions. [Pg.158]

Considering the simplest carbene, methylene, it is clear that it could have a linear structure (D -symmetry) or be bent ((72s-symmetry). In the former case, using the ls-orbitals of hydrogen and the 2s- and 2 -orbitals of carbon, two a molecular orbitals can be constructed and these can clearly accommodate the C—H bond electrons. A degenerate pair of orbitals, similar to carbon atomic p-orbitals, are the ones of next-lowest energy. The linear structure of methylene would thus correspond to a triplet state. [Pg.158]

Bending the linear CH2 molecule should have little effect on the p-type orbital perpendicular to the plane of bending, which now becomes [Pg.158]

On this basis a substantial number of not wholly conclusive attempts have been made to treat methylene theoretically. Both VB and MO approximations have been used, but, in particular, there has been no consensus of theoretical opinion as to whether the ground state of methylene is a singlet or a triplet. The literature up to 1964 has been critically reviewed by Gaspar and Hammond (1964). [Pg.158]

The basic theoretical concepts describing the interaction of a sufficiently massive and energetic particle with a surface are the binary collision (BC) model and the molecular or classical dynamics (MD) model. [Pg.343]

The interaction of an ion or atom with another atom leads to an exchange of momentum and energy. Conservation of momentum and energy requires that the total momentum and the total energy be the same before and after each collision i.e., for a target atom initially at rest, [Pg.343]

For one collision partner at rest prior to the collision, the kinematics are depicted in Fig. 2. The exact amounts of transferred momentum and energy depend on the details of the collision, for example, impact parameter b and scattering angle 6. In the laboratory system, the energies E] and E2 of the projectile and the target atom, respectively, after the collision are given as [Pg.344]

The maximum energy transferred from the projectile to a target atom is [Pg.345]

The scattering angles depend not only on the collision parameters-for example, the impact parameter Z)-but also on the interaction potential V(r). Particularly at low relative velocities of the colliding partners, a proper choice of the interaction potential may become crucial. In the center-of-mass system, the scattering angle 0cm lay be obtained as [Pg.345]

Theoretical Considerations.—Calculations (CNDO/2, ab initio) on thiiren indicate that 3d-orbital participation is likely to be unimportant in the structure and bonding. Calculations on thiiren 1-oxide indicate an inversion barrier of ca. 20 kcal mol. The inversion barrier for S-protonated thiiren is calculated as 85 kcal mor. Thiiren is compared with azirine and oxiren. Other calculations (MINDO/3 and NDDO) on thiiren indicate that it should be relatively stable (heat of formation 205.4 kJ moT ) and that thiirens may be reasonable intermediates in reactions. Heats of formation of oxiren, IH-azirine, cyclopropene, and the cyclopropenyl anion were calculated also. Thiiren is predicted to be more stable than the acyclic, isomeric carbene (119), the zwitterion (120), and the cyclic zwitterion-carbene [Pg.110]

Intermediates in Reactions.—Attempts to prepare metal complexes of thiirens resulted in the formation of complexes of thioketocarbenes instead. Treatment of 1,2,3-thiadiazoles and -selenadiazoles with di-iron enneacarbonyl gives thioketo- and selenoketo-carbene complexes. The formation of two carbene complexes from unsymmetrically substituted thia- or selena-diazoles suggests the intermediacy of a thiiren or seleniren complex.  [Pg.110]

V Symposium Organic Sulfur Chemistry, Lund, Sweden, June, 1972, Intemat. J. Sulfur Chem. (C), 1972, 7, 11. [Pg.110]

Thiirenium ions were invoked as intermediates to explain the enhanced rate of solvolysis of trans-l,2-dimethyl-2-methylthiovinyl 2,4,6-trinitro-benzenesulphonate, in substitution reactions of -phenylthiovinyl sul-phonates, and in additions of benzenesulphenyl chloride to diacetylenes. Rationalizations of the mass spectra of various sulphur-containing five- and six-membered cyclic compounds have involved thiirenium ions.  [Pg.111]

Support was obtained for the intermediacy of thiiren 1,1-dioxides in the reacti(m of aa-dihalogeno-sulphones With base to yield a 3-unsaturated sulphonic acids. [Pg.111]

The major theoretical considerations in the Haber process are related to the position of equilibrium of the strongly exothermic reaction. [Pg.144]

Such a reaction is favoured by low temperatures, at which reaction rate is slow, however. Catalysts are therefore required to increase the speed of the reaction. [Pg.144]

By Le Chatelier s principle it is clear that the exothermic reaction is favoured by low temperatures, and since 4 gaseous moles go to 2 gaseous moles, ammonia formation is also encouraged by high pressure. The effect of temperature and pressure on the equilibrium is shown in Table 3.5. [Pg.144]

Theoretically the optimum temperature and pressure are 200 °C and 600 atmospheres. However, in modern plant, since recycling is possible, such stringent conditions are not economically viable. In practice in conventional plant temperatures and pressures of 400 °C and 200 atmospheres are more realistic. In the AMV process similar conversions are achieved at much lower pressure (80 atmospheres). In neither case is the reaction allowed to reach equilibrium, and the resulting conversion is only about 14-15% by volume of ammonia, but this is compensated for by recycling. [Pg.144]

The factors affecting the choice of catalyst are cost and efficacy. In the Haber process the main catalyst used has been iron with potassium hydroxide as promoter. In the AMV process the iron catalyst has been improved with a new combination of promoters which gives longer life and higher activity. Many catalysts can easily be poisoned and iron is no exception. It is poisoned by H2O vapour, H2S, CO and CO2, and therefore these must be excluded from the process if long life is to be assured. [Pg.144]

The apparent simplicity of the H—Si system has enabled a few realistic theoretical treatments of chemisorption on semiconductors to be made. The details of the calculations are outside the scope of this article, but it will be useful to summarize some of the principal conclusions. [Pg.231]

Appelbaum and Hamann [209] produced a fully self-consistent first principles calculation for the chemisorption of H on Si lll, which showed that the Si—H bond potential is considerably greater than that for Si—Si. The force on the H atom is small and inward, with a bond length of 2.73 0.02 a.u. The Si-H bond force constant is 0.175a.u. compared with the measured value of 0.173 a.u. for SiH4. The corresponding surface phonon, as mentioned previously, has been observed by ELS [214]. In the calculated electronic structure of the Si—H surface, the most notable feature is the disappearance of states in the fundamental band gap and the corresponding appearance of a band of states, clearly connected with the Si- H bond, in the gap between the second and third valence bands. [Pg.231]

To accommodate the H-donated electron, the clean surfaces dangling bond orbital must promote an electron into the bridge bond orbital which is empty for the clean surface, lying just above the dangling bond orbital. [Pg.232]

Although the calculation was for Si 100, it may be applicable to any Si surface whose second layer is roughly tetrahedrally coordinated. This type of bond could also be the precursor state for the corrosive modification of hydrogenated Si surfaces. [Pg.232]

Recent experimental and theoretical work has produced a rather clear understanding, albeit with some speculation, of the electronic processes involved in the chemisorption of H atoms on the low index surfaces of silicon. Even these very simple systems exhibit complicating features, however, and it is probably unrealistic to expect such detailed models to be available for any other gas-isemiconductor combination. Nevertheless, we will discuss in the following three sections the results which have been obtained at the next level of complexity, viz. oxygen on Si and GaAs, and chlorine on Si. [Pg.232]

The Structure of Small Metal Particles (a) Theoretical Considerations. - [Pg.154]

Julg et al.24 employed an approximation based on the self consistent field molecular orbital method to evaluate the average energy per atom for various structures. They calculate that whereas the normal b.c.c. structure is more stable for clusters containing more than 106 atoms, smaller clusters prefer to take up pentagonal symmetry. However, these authors make an important point, namely, that the calculated energies for different structures are very similar. Interconversion of different structures will be facile, and external factors such as the method of deposition, level of impurities, support effects, etc., may cause the less stable structure to grow. For example, impurities on [Pg.154]

Wynblatt and N. A. Gjostein, Prog. Solid State Chem., 1975, 9, 21. [Pg.154]

Baetzold and Hamilton31 recently have reviewed the quantum chemical theoretical models used to compare the stability of different structures of small metal particles. Only a brief summary is given here. [Pg.155]

More recent calculations, however, which allow for more spd hybridization indicate a preference for three-dimensional structures.31 The new calculations show the delicate balance between the various geometries. Calculations for [Pg.155]

The behavior of pyridine, its i T-oxide, and its quaternary salts has been the subject of a number of recent theoretical treatments.1-4 The general conclusions will be summarized here to serve as a guideline on which to superimpose the effect of substituent groups. [Pg.230]

Substitution of =N— for ==CH— in benzene is accompanied by considerable deactivation toward electrophilic substitution, the effect being felt least at C-3 and most at C-2 and C-4. Both the 77-electron density and the localization energy treatments agree on this point. It has been estimated5 that substitution of =N— is deactivating by a [Pg.230]

in Physical Methods in Heterocyclic Chemistry (A. R. Katritzky, ed.), Vol. I, Chapter 2, p. 109. Academic Press, New York, 1963. [Pg.230]

Zahradnik and C. Pdrkanyi, Collection Czech. Chem. Commun. 30, 355 (1965). [Pg.230]

The various theoretical approaches agree with the simple resonance theory representation of the valence structure of pyridine in predicting that nucleophilic substitution should take place readily at the 2-, 4-, or 6-positions but not at the 3- or the 5-position. [Pg.231]

Electrocatalytic Aspects of Dioxygen Reduction 3.3.4.1 Theoretical Considerations [Pg.241]

One of the primary aims from an experimental viewpoint is to identify the rate determining step and implement methodologies that can afford values for the kinetic rate constants involved. The mathematical analysis of data collected with the RD E and [Pg.241]

at sufficiently negative potentials, so that the macrocycle will be present solely in its active reduced form, a plot of ln[(i — iLev)/i] versus E (or Tafel plots) would be linear with a slope of a F/RT, yielding, for a = 0.5, a value of about 120 mV per decade. [Pg.243]

It thus follows that at sufficiently negative potentials, the kinetic current, ikin and, hence, the measured current, i, will be a maximum, to be denoted as ij and imax, respectively. If it is further assumed that (a) the kinetics associated with the redox process involving the bound catalyst are very fast so that the relative concentrations of [Pg.243]

It becomes evident from this last expression that E°22 will shift toward more positive values as i , or equivalently, the magnitude of the rate constant of association k2 is increased. It is conceivable that the half-wave potential for the oxygen reduction reaction can be shifted by as much as 100 mV from E rf however, larger shifts are not likely, as a subsequent electron transfer step may become rate-limiting. [Pg.244]

Ledwith and D. C. Sherrington C. Conductance and Ion Pair Equilibria C.l. Theoretical Considerations [Pg.6]

Today it is widely accepted that any organic salt. A+ ET, may exist in a number of aggregated forms in solution as shown below. [Pg.6]

2A+ (solv.) + 2B (solv.) 2[A+ (solv.)B ] — 2[A+...B ]. Free solvated ions Loose ion pairs Tight ion pairs [Pg.6]

P and Q are constants defined by the dielectric constant D and viscosity t] of the solvent and the prevailing temperature T, and X0 is the limiting conductance at infinite dilution. [Pg.6]

Fuoss (40) has improved Bjerrum s original treatment (37) of this situation and, although a number of other sophistications have been introduced, his formulation (41) is the one most used today. In fact rather fortuitously the relatively low dielectric constants of solvents employed in organic chemical reactions, particularly ionic polymerisations, are ideal media for the application of these theories. The analysis carried out by Fuoss leads not surprisingly to an equation [Pg.6]

We take up here some aspects of the thermodynamics of adsorption that are of special relevance to gas adsorption. Two types of processes are of interest  [Pg.641]

If the process is carried out at constant volume, the heat evolved Qi will be equal to an energy change AE2 or, per mole of adsorbate, qi = Ae2 (small capital letters will be used to denote mean molar quantities). Alternatively, the process may be [Pg.642]

The heat evolved will now be a differential heat of adsorption, equal at constant volume to Qd or per mole, to qd - AI2, where Ae2 is the change in partial molar energy. It follows that [Pg.642]

Adsorption Heats and Entropies. It is not necessary, phenomenologically, to state whether the process is adsorption, absorption, or solution, and for the adsorbent-adsorbate complex formal equations can be written, such as [Pg.642]

However, a body of thermodynamic treatment has been developed on the basis that the adsorbent is inert and with attention focused entirely on the adsorbate. The abbreviated presentation given here is based on that of Hill (see Refs. 65 and 113) and of Everett [114]. First, we have the defining relationships  [Pg.642]

It is apparent that the existence of a second-order term in the rate expression does not of itself offer any proof of associative or dissociative activation, for there are two possible alternative mechanisms compatible. These are  [Pg.43]

Alternative (ii) corresponds to the [Re(CO)4X]2 case, equations (41) and (42) above. However, it was here favoured largely because no second-order term was observed for the Re(CO)5X and Re(CO)4LX substitution. In the case of Mo(CO)5Py, expected to be closely similar to Mo (CO)4dipy, a second-order dependence has been observed. [Pg.43]

In the final section of this chapter, we shall attempt to give a brief rationalization of the regularities and peculiarities of the reactions of non-labile complexes which have been discussed in the previous sections. The theoretical framework in which the discussion will be conducted is that of molecular orbital theory (mot). The MOT is to be preferred to alternative approaches for it allows consideration of all of the semi-quantitative results of crystal field theory without sacrifice of interest in the bonding system in the complex. In this enterprise we note the apt remark d Kinetics is like medicine or linguistics, it is interesting, it js useful, but it is too early to expect to understand much of it . The electronic theory of reactivity remains in a fairly primitive state. However, theoretical considerations may not safely be ignored. They have proved a valuable stimulus to incisive experiment. [Pg.43]

Two remarkably successful generalizations from the preceding pages deserve attention first of all. Octahedral complexes show a pronounced tendency to react [Pg.43]

11 and 12 show typical mo diagrams for square planar and octahedral complexes. Inspection reveals that the metal orbital (z is the axial direction) in a square planar complex is involved in the n bonding system and available for a bonding in the transition state. This is a feature shared by nucleophilic substitution at square planar complexes with the spectacularly associative nucleophilic aromatic substitutions. The octahedral complexes discussed in this chapter [Pg.44]

The theory of premixed flames essentially consists of an analysis of factors such as mass diffusion, heat diffusion, and the reaction mechanisms as they affect the rate of homogeneous reactions taking place. Inasmuch as the primary mixing processes of fuel and oxidizer appear to dominate the burning processes in diffusion flames, the theories emphasize the rates of mixing (diffusion) in deriving the characteristics of such flames. [Pg.318]

It can be verified easily by experiments that in an ethylene-oxygen premixed flame, the average rate of consumption of reactants is about 4 mol/ cm3 s, whereas for the diffusion flame (by measurement of flow, flame height, [Pg.318]

FIGURE 6.8 Balances across a differential element within a diffusion flame. [Pg.319]

The theoretical solution to the diffusion flame problem is best approached in the overall sense of a steady flowing gaseous system in which both the diffusion and chemical processes play a role. Even in the burning of liquid droplets, a fuel flow due to evaporation exists. This approach is much the same as that presented in Chapter 4, Section C2, except that the fuel and oxidizer are diffusing in opposite directions and in stoichiometric proportions relative to each other. If one selects a differential element along the x-direction of diffusion, the conservation balances for heat and mass may be obtained for the fluxes, as shown in Fig. 6.8. [Pg.319]

In Fig. 6.8, j is the mass flux as given by a representation of Fick s law when there is bulk movement. From Fick s law [Pg.319]

Macromolecules, e.g., proteins, need a distinct structure within the aqueous surrounding to realize their biologic functions. This structure is stabilized inter-alia by ionic interactions between positively and negatively charged amino acid side chains and between these chains and other molecules. Optimal functionality needs a well-balanced ratio of charged residues. Each disorder of this ratio results in alterations up to complete denaturation. [Pg.191]

Since the side chains of a distinct amino acid do not show complete dissociation at common concentrations, these acids (when forming an anion during dissociation) and bases (when forming a cation) are called weak acids and bases, respectively, as opposed to the completely dissociated strong acids and bases, e.g., hydrochloric acid, trifluoroacetic acid, sodium hydroxide, or triethylammonium hydroxide. [Pg.191]

Weak acids and bases are not restricted to amino adds many other compounds also behave similar in aqueous solutions. The dissociation into anion A and proton (in aqueous solution the dissociated protein is captured by a water molecule to form a hydronium ion HsO ) in the case of acids, and the addition of a proton to a base B to form the cation BH , is an equilibrium [Pg.191]

This equilibrium can be described for dissociation by the thermodynamic equation  [Pg.191]

In a more detailed view are factors of the equilibrium equation, not the concentrations, but the activities ax, i.e., only a part of the total amount of a reactant  [Pg.191]

For most of the resins used in RTM the flow through the reinforcement is governed by Darcy s law. Deviations from this law can be expected if the resin is non-Newtonian or if the reinforcement is displaced by the mold filling. The qualitative behavior, however, will generally be as follows. [Pg.365]

For flow in one direction Darcy s law predicts that the flow rate per unit area (Q/A) is proportional to the pressure gradient (Ap/L), and inversely proportional to the viscosity of the resin (p)  [Pg.366]

The coefficient of proportionality K is called the permeability of the reinforcement. According to theory [5] K is only dependent on the geometry between the fibers in the reinforcement (the pore space ). Several models for the dependence of K on the fiber volume fraction Vf has been proposed. The most-cited model is the so-called Kozeny-Carman model [16,17], which predicts a quadratic dependence on the fiber radius R in addition to the dependence on Vf [Pg.366]

The constant k is called the Kozeny constant and it attains a value of 0.7 for well-ordered reinforcements with uniformly distributed fibers, (e.g. unidirectional prepreg) [17]. For commonly used fabrics in LCM (e.g., continuous strand mat or weaves) R2/4k should be seen as an adjustable model parameter with only weak coupling to the fiber or fiber bundle diameter. [Pg.366]

Continuous strand mats are approximately isotropic and have almost the same permeability in all directions (in the plane of the fabric). Many other fabrics, however, are strongly anisotropic and have different permeability in different directions. Gebart [18] proposed a model for this class of fabrics derived theoretically from a simplified fiber architecture. The model, which is valid for medium to high fiber volume fractions, was developed for unidirectional fabrics, but it can also be used for other strongly anisotropic fabrics. In this model the permeability in the high permeability direction (which is usually, but not always, in the direction of the majority of fibers) follows the Kozeny-Carman equation (Eq. 12.2). In the perpendicular direction, however, it is  [Pg.366]

The important concept for scale-up is the principle of similarity (1-6). When scaling up any mixer/granulator (e.g., planetary mixer, high-speed mixer, pelletizing dish, etc.), the following three types of similarity need to be considered geometric, kinematic, and dynamic. Two systems are geometrically similar when the ratio of the linear dimensions of the small-scale and scaled-up system are constant. [Pg.200]

Two systems of different size are kinematically similar when, in addition to the systems being geometrically similar, the ratio of velocities between corresponding points in the two systems are equal. Two systems of different size are dynamically similar when in addition to the systems being geometrically and kinematically similar, the ratio of forces between corresponding points in the two systems are equal. [Pg.200]

Both methods yield dimensionless groups, which correspond to dimensionless numbers (1), e.g.. Re, Reynolds number Fr, Froude number Nu, Nusselt number Sh, Sherwood number Sc, Schmidt number etc. (2). The classical principle of similarity can then be expressed by an equation of the form  [Pg.200]

This equation may be a mechanistic (case A) or an empirical one (case B)  [Pg.201]

The unknown parameters a, b, and c are usually determined by nonlinear regression calculus. [Pg.201]

There are several consequences of this effect in gold chemistry  [Pg.3]

The color of gold. Gold has an absorption beginning at 2.4 eV, attributed to a transition from the filled 5d band to the Fermi level (essentially the 6s band). It therefore reflects red and yellow light and strongly absorbs blue and violet. The analogous absorption for silver, however, lies in the ultraviolet, at around 3.7 eV. [Pg.3]

Some qualitative comments were made about the velocity autocorrelation function in Chap. 8, Sect. 2.1. In this section, it is considered in more quantitative detail. One of the simplest expressions for the diffusion coefficient is that due to Einstein [514]. He found that a particle executing a random walk has an average mean square displacement of (r2 after a time t, such that [Pg.321]

The average is taken over all possible configurations that the system of interest can assume (i.e. weighted by the Boltzman factor). Now, the displacement of a particle from its initial position, r, is where [Pg.321]

Because the fluid is in equilibrium, any ensemble average property should not change with time. Hence, the ensemble average of (u(tf)u(t ) depends only on the relative difference of time, t — t . That is, it is a stationary process. On transforming the time variables to f and r = tr — f (rather like the centre of diffusion coefficient transformation of Chap. 9, Sect. 2), the Green—Kubo expression for the diffusion coefficient is obtained [453, 490], [Pg.321]

It shows the clear link between the change of motion of the particle and its diffusion coefficient. In Fig. 50, the velocity autocorrelation function of liquid argon at 90 K (calculated by computer simulation) is shown [451], The velocity becomes effectively randomised within a time less than lps. Further comments on the velocity autocorrelation functions obtained by computer simulation are reserved until the next sub-section. Because the velocity autocorrelation function of molecular liquids is small for times of a picosecond or more, the diffusion coefficient defined in the limit above is effectively established and constant. Consequently, the diffusion equation becomes a reasonable description of molecular motion over times comparable with or greater than the time over which the velocity autocorrelation function had decayed effectively to zero. Under [Pg.321]

From the considerations above, a further semi-quantitative observation can be made about molecular motion. Over short times, the velocity of motion of a molecule is correlated with its velocity a little earlier. Under these circumstances, the mean square displacement is of the form [Pg.322]

The effects of various factors such as pH, the common ion effect, and temperature on solubility will have a greater impact on formulation development for insoluble compounds than for soluble ones. The general solubility theory has been extensively discussed in the literature (James, 1986 Grant and Higuchi, 1990). To afford better understanding of the solubility behavior of insoluble compounds, the pertinent solubility theory and its practical implications will be reviewed here. [Pg.63]

If a catalyst surface is exposed to a reaction gas mixture, heat is produced in exothermic reactions and consumed in endothermic reactions. The amount of heat produced will be proportional to the linear combination of catalytic activity and the enthalpy of all occurring reactions  [Pg.176]

If side and sequential reactions have been excluded, the heat should be proportional to the enthalpy of the desired reaction  [Pg.176]

Because the spatial area with higher temperature on the catalyst surface of one of the samples of the library is very small the detection of catalytic activities through temperature measurement cannot be carried out by direct temperature measurements but only by non-contact methods such as pyrometry or IRT. The IR video camera used here measures the emission at every point of the library in parallel. The detector consists of a 256x256 pixel array of Pt-silicide-IR-sensors. Each pixel delivers a voltage-signal that depends on the infrared radiation and the sensitivity of that pixel (fixed pattern noise). [Pg.177]

To calibrate the pixel sensitivities black body radiation is usually measured at different temperatures. Since a black body has an emissivity of 1 at every position, variations in detector pixel sensitivities are eliminated by a calibration function. As this IRT-method should be used here to quantify very small heat signals on combinatorial libraries with diverse materials, differences in emissivities have to be considered. Most materials are grey bodies with individual emissivities less than 1. Therefore, the calibration was not performed with a black body but with the library, as described before, a procedure that corrects not only for pixel sensitivity but also for emissivity differences across the library plate [5]. For additional temperature calibration, the IR-emission of the library is recorded at several temperatures in a narrow temperature window around the planned reaction temperature. By this procedure, emissivity changes, temperature dependence and individual sensitivities of the detector pixels can be calibrated in one step. After this [Pg.177]

The partitioning phenomenon is the most elementary model used to describe DOM-HOC interactions it can be quantified using a simple equilibrium type relationship [Pg.163]

The Flory parameter is in essence analogous to the activity coefficient of the HOC in the DOM phase and consists of two components %u and 5Cs which are the enthalpic and entropic contributions, respectively  [Pg.164]

The Xh term quantifies the nonideal heat of mixing between the HOC and DOM phase and is typically quantified using the one-solubility parameter Scatchard-Hildebrand equation [Pg.164]

One limitation of the one-solubility parameter model is that it assumes that the solute can only interact with the organic matter through London forces. Although this assumption may be reasonable for SOM, DOM is typically more polar and can participate in other types of van der Waals interactions. These include permanent dipole-induced dipole (Debye) and permanent dipole-permanent dipole (Keesom) interactions in which the degree of binding that occurs depends on the polarizability of the DOM (Gauthier et al., 1987 Uhle et al., 1999). To account for these types of interactions Chin and Weber (1989) segregated the solubility parameter terms into three components to account for all these different types of molecular interactions to [Pg.165]

PMA was selected based upon structural similarities between it and some types of DOM (Spiteller and Schnitzer, 1983). Recently, however, several investigators have demonstrated that PMA may not have as many structural similarities to DOM (specifically fulvic acids) as once believed (Hess and Chin, 1996 Kilduff et al., 1996). These new data may explain, in part, the poorer estimates of Kdom reported by Chin and Weber (1989) [Pg.165]

T-C is the interface between gas and liquid. Each point on the line corresponds to a certain temperature and the pressure needed to liquefy the gas at this temperature. Point C is the critical point. Beyond the critical temperature, a gas does not liquefy under increasing pressure. Instead, it is compressed into a supercritical fluid. The critical point is substance-specific. Table 3.2 shows the supercritical conditions of some selected solvents. [Pg.149]

Substance Critical Temperature (°C) Critical Pressure (atm) Critical Density (103 kg/m3) [Pg.149]

Reproduced from Ref. 24, with permission from Kluwer Academic Publishers. [Pg.149]

State Conditions0 Density (103 kg/m3) Viscosity (mPa-s) Self-Diffusion Coefficient (104 m2/s) [Pg.150]

Sample volume is the most fundamental factor to be taken into account when designing an HPLC system in which a small-volume column is used, [Pg.245]

The concept of maximum sample volume as it relates to miniaturization can be illustrated as follows, assuming that both a conventional analytical column (4.6 mm I.D.) and a narrow-bore column (2 mm I.D.) have equal efficiency, length, and porosity. To switch a method from the analytical column to the narrow-bore column and still maintain optimum performance on the narrow-bore column, Eq. (8.1) may be rewritten as [Pg.246]

Vs should be 4.8 times smaller to ensure a similar column performance and to avoid any loss in column efficiency. Similarly, the sample volume should be 21 times smaller for a microbore column with an inner diameter of 1 mm. [Pg.246]

Reducing the sample volume, however, means that the mass of sample loaded onto the narrow-bore column is reduced, and therefore the mass of sample reaching the detector is decreased. This imposes difficulties on the detection scheme because less sample is available for detection. Therefore, it is important that the entire instrument be optimized for use with small-bore columns. Examples of reduced sample volumes for each of the column categories are listed in Table 8.2. [Pg.246]

Although chromatography is a separation process, dilution occurs during the process of separation. The small sample volume that is injected onto the head of the column disperses in the mobile phase during passage through the column. The dilution factor can be expressed in terms of the maximum peak concentration, Cmax, and is related to the injected sample mass, ms, according to [Pg.246]

Great progress has been made in understanding infrared spectra and in the contributions which they make to molecular structure but we shall have to confine ourselves to those fields which may have a possible bearing on chemical reactivity. [Pg.216]

Speaking specifically of ethyl bromide, the energy of activation calculated from the temperature coefficient of the thermal dis- [Pg.217]

There is considerable support for the hypothesis that a molecule decomposes unimolecularly when a sufficient amount of energy becomes localized in a particular bond or mode of vibration.19 Knowing these various types of vibration as in the ethyl bromide molecule one is tempted to speculate as to which are the most likely ones to be involved in the chemical reaction. For example, if ethyl bromide decomposes to give a free ethyl radical and a bromine atom as the first step the action must occur by increasing the amplitude of vibration of the fundamental frequency Fi to the point of rupture. On the other hand if the molecule disrupts into ethylene and hydrobromic acid in a single internal operation the fundamental frequency Fq or F8 must be involved. These latter [Pg.218]

The direct significance of these fundamental frequencies in chemical reactions is speculative the determinations of these values has more practical importance along two other lines. They are used together with other constants for calculating activation energies as shown in the next chapter, and they are used to determine the presence or absence of intermediate complexes or loose chemical compounds in solution. Combination of solute with the solvent can be determined by slight displacement of the low frequencies as revealed from infrared or Raman spectra and these facts will be of ultimate value in predicting reaction rates in solution. [Pg.219]

If one accepts the above small modification of the Flory model for equilibrium swelling, and also assumes that the turgid end-state is described by the van t Hoff relationship  [Pg.21]

The relative swelling power, C, of the sorbed liquid is the product of two factors, namely the number, a, of adsorbed molecules per accessible monomer unit of polymer at liquid-saturation, and p, i.e. (M/dp)/(Mpd) where M and Mp are the formula weights of the sorbed liquid and monomer unit of polymer respectively and d and dp are the respective densities of the liquid and polymer. From the standpoint of interpretation of polymer swelling in terms of molecular structure, a is more meaningful than C, from which a can be calculated by means of Eq. 15. [Pg.22]

Since the adsorbed molecules are in exchange equilibrium with the rest of the sorbed molecules, a is in effect the average dynamic packing density of the molecules immobilized by adsorption to the accessible monomer units of crosslinked polymer at liquid saturation. If the relationship expressed by Eq. 14 is indeed correct as [Pg.22]

To account for the possible contribution of cyclohexane-1,4-diyl, we must include the configuration arising from the excitation of the electrons from the HOMO to the LUMO. Thus, the diyl Slater determinant T djyi is [Pg.218]

The last contribution comes from the bis-allyl supermolecule. This structure arises from removing the electrons from 5a and placing them into 5b [Pg.219]

An HF wavefunction includes only therefore minimizes the contribu- [Pg.219]

11 — CURRENT DEVELOPMENTS AND FUTURE RESEARCH IN CATALYTIC MEMBRANE REACTORS [Pg.550]

At steady-state Becker et al. [116] write the following set of equations. [Pg.550]

Equations (11.1)-(11.4) are complemented by a set of corresponding initial and boundary conditions. [Pg.551]

The model of Tayakout et al. [117,118] in addition accounts for the possibility of axial dispersion effects in the tubeside and shellside. The inclusion of axial dispersion effects in regions (1) and (4) necessitates a different set of initial conditions at Z = 0 and a companion set of conditions at Z = L. The effect of pressure drop through the catalytic bed could be included in this type of model using Ergun s equation. [Pg.553]

From an economic perspective both the compulsory and promoting elements of activation contribute to a strengthening of work incentives, return from employment relative to benefit receipt and - in the end - imply a behavioural change. In all countries, activation instruments such as integration contracts or activation programmes incorporate both demanding and enabling elements simultaneously. [Pg.417]

Both types of measures aim at increasing the job search intensity of the unemployed. However, support and compulsion induce not the same effects on wage and employment concessions an unemployed is willing to make. The compulsory effect will directly increase the willingness to make concessions (e.g. by raising search and availability requirements or testing the motivation by offering unpleasant measures) while the supportive effect will most probably increase the human capital and search effectiveness and hence reduce the necessity of concessions by the unemployed. However, it is an empirical question which effect dominates. [Pg.417]

While treatment effects do not differ regardless of whether participation is voluntary or mandatory, there is an additional threat or motivation effect only when participation is mandatory. The threat of being required to participate in an activation programme motivates the unemployed to search more actively for a job, and hence this threat or motivation effect is conducive to accelerated job finding. However, the net effect on search intensity among those without a job is theoretically ambiguous The potentially negative lock-in effect for the activated and the positive threat/motivation effect for the unemployed have to be analysed empirically to find out which effect dominates. [Pg.417]

Finally, the effects of activation pohcies on unemployment should be seen relative to the resources spent on administration and programme activities. These resources have to be financed via taxes which, in turn, can result in distorting effects on the labour market. Hence, a reduction in unemployment - open and total - may be achieved at a too high cost. The country studies show that the use of compulsory elements in unemployment insurance and social policies implies that active labour market policies are used much more intensively and that additional resources have to be dedicated to programme activities. [Pg.418]

The angular frequency a denotes hereby the frequency a = 2%f. Beyond the frequency of transition f the device is not able to efficiently drive a second transistor of the same kind. Generally, no circuitry of such transistors can operate beyond  [Pg.488]

The eontribution to the drain current from the gate drain capacitance was found to be small for frequencies within the unity-gain bandwidth and is therefore ignored. The gate current becomes  [Pg.489]

The drain-source capacitance Qs can be neglected since only a constant drain voltage Vis is applied. The total gate capacitance is given by Cg = tot Q with yf tot ihs total gate area. The unity-gain bandwidth can now be calculated from Eqs. (8), (10) and (12)  [Pg.489]

In combination with Eqs. (15) and (16), the transfer frequency can be expressed in terms of the structural layout parameters B, Aq and JV as  [Pg.490]

According to Eq. (18) it is obvious how the transfer frequency can be increased by the layout. Mainly the channel length L allows higher to be achieved. The minimisation of this parameter is therefore the major goal, as [Pg.490]

The size distribution of aerosol particles was presented in Subsection 4.3.2. We have not discussed, however, the relation between the size distribution and the relative humidity of the air, since for such a discussion the knowledge of the chemical composition is necessary. The aim of this section is to summarize the problem with the presentation of some results of measurements. The interested reader is referred for further details to Hanel (1976). [Pg.128]

Schematic variation of the radius (r) of a soluble particle as a function of relative humidity of the air. r0  [Pg.128]

It is known from physical chemistry that the equilibrium vapour pressure is smaller over solutions than over pure water. In the case of ideal solutions this vapour pressure decrease is proportional to x0, the mole fraction of the solvent (Raoult s law). If the solution is real, the interaction of solvent and solute molecules cannot be neglected. For this reason a correction factor has to be applied to calculate the vapour pressure lowering. This correction factor is the so-called osmotic coefficient of water (g ). We also have to take into account that the soluble substance dissociates into ions, forming an electrolyte. [Pg.129]

If we further raise the relative humidity after the phase change (see Fig. 37) the radius of the droplet increases and the solution becomes weaker and weaker. This means that at higher relative humidity a more dilute solution is in dynamic equilibrium with the vapour environment. It should be mentioned that the equilibrium radius is governed also by the curvature of the droplet. Since the relation between the curvature and droplet radius is given by the well-known Thomson equation, we may write (Dufour and Defay, 1963 E. Meszaros, 1969)  [Pg.129]

After a simple mathematical transformation equation [4.13] yields [Pg.129]

A Hiickel molecular orbital (HMO) model has been used to explain some of the characteristic properties of dihydrodiazepines.29 The authors assumed that there was conjugative interaction between positions 4, 5, 6, 7, and 1 on the dihydrodiazepine ring but no N, N lone pair interaction. The results obtained by this model are given in Table II. [Pg.9]

HMO Data and Wavenumbers for Long-Wavelength Transitions of Some Dihydrodiazepinium Perchlorates, and Chemical Shift Parameters [Pg.10]

0 For explanation of terms, see text. 6 Sh measured in trifluoroacetic acid. [Pg.10]

Dihydrodiazepinium salts are characterized by intense absorption bands (t = 15,000-25,000) lying between 300 and 360 nm.)ilwi These high absorption values are indicative of ir-ir transitions, and this is substantiated in some cases by the presence of n-ir transitions on their long-wavelength side.30 31 [Pg.10]

The relationship between the wavenumbers ( ) of these transitions and Am, the difference between the parameters of the lowest unoccupied MO, mm+1, and the highest filled MO, mm, have been tested.29 A plot of v against Am for some ten dihydrodiazepinium perchlorates illustrates the essential distinction in compound type between these salts depending on whether there are exocyclic phenyl groups or methyl groups at position 5(7), presumably because of conjugative interaction in the case of the 5(7)-phenyl substituents. [Pg.10]

The fundamental parameter used to characterize the position of a sample zone in a thin-layer chromatogram is the retardation factor, or Rp value. It represents the ratio of the distance migrated by the sample compared to the distance traveled by the solvent front, and for linear development is given by Eq. (6.1) [Pg.504]

Rp values are generally calculated to two decimal places. Some authors prefer to tabulate values as whole numbers, as hRp values equivalent to 100 Rp. The Rp value is not linearly related to the distribution properties of the separation system. The Rm value is used in studies that attempt to correlate migration properties to solute structure. The Rm value is equivalent to the ratio of the residence time of the solute in the stationary and mobile phases, and is formally equivalent to the retention factor (log k) in column liquid chromatography. It is calculated from the Rp value by Rm (or log k) = log [(1 - [Pg.505]

The common methods of mobile phase transport through the layer are capillary action, forced flow, and electroosmosis. Ease of implementation results in capillary flow [Pg.505]

The velocity constant, k, is related to the experimental conditions by equation (6.2) [Pg.506]

An alternative approach to forced flow is to seal the layer with a flexible membrane or an optically flat, rigid surface under hydraulic pressure, and to deliver the mobile phase to the layer by a pump [9,41,43-46]. Adjusting the solvent volume delivered to the layer optimizes the mobile phase velocity. In the linear development mode, the mobile phase velocity (uf) will be constant and the position of the solvent front (Zf) at any time (t) after the start of development is described by Zf = Uft. The mobile phase velocity no longer depends on the contact angle and solvent selection is unrestricted for reversed-phase layers in forced flow, unlike capillary flow systems. [Pg.508]

The flux J of fluid across a membrane free of deposited materials may be described by Darcy s law i.e. [Pg.178]

While size reduction or blockage of pores may be considered to increase the resistance of the membrane (Rm) to permeate flux, accumulation of materials in the cake and concentration-polarization layers (so-called polarised solids) presents additional resistances to permeation (denoted here as R c and Rep respectively). These resistances var) as a function of the composition and thickness of each layer, which in turn are determined by the feed water quality and the characteristics of mass transfer in the membrane module. In most instances encountered in water and wastewater treatment, it appears that the concentration-polarisation layer, if it is formed, contributes negligible resistance to permeate flux i.e. Rep Rc and, therefore. Rep may be neglected (Mallevialle et al (1996)). While this is in reality not always the case (as shown in later sections of this chapter and in Chapter 7) for the filtration of [Pg.178]

According to filtration theor) (Bowen and Jenner (1995)), the resistance of cake solids (assuming solids in the concentration-polarisation layer to be negligible) can be written as [Pg.179]

Since the single pardcles with a mean diameter of 70 nm are too large to penetrate the membrane pores which have an estimated pore size of less than 10 nm (Cheryan (1986)), separadon of the total resistance into the intrinsic membrane resistance and the resistance due to the hydraulic resistance of the filtradon cake would seem reasonable. A high hydraulic cake resistance is observed for concentradons between 0 and 60 mM KCl and a lower hydraulic resistance for concentrations higher than 70 mM. A distinct break between these two regimes is observed at around 65 mM KCl. [Pg.180]

Solution Composition Initial Flux [Lm%i] Flux (2.8 L) [Lm-%- ] Membrane Resistance [10 m- l Total Resistance [10 m- ] Cake Resistance [10 m- l [Pg.181]

This classification, valid for concerted cis-cis (or supra,supra) processes, confirmed that thermal Diels-Alder reactions (m-f-/i = 6) can be (but not, must be) one-step reactions, while predicting that photochemical 1,4-cyclo-additions should be multistep reactions 1,3-cycloadditions should behave analogously, since 1,3-dipoles are four 7r-electron systems. Common 1,2- [Pg.152]

Also cis-trans ov supra,antara) cycloadditions of some 7r-electron systems are sterically feasible (ie. the top face of one component reacts with the bottom face of the other, at one side, but the two bottom faces react with each other at the other side of the cycloaddition). In such cases the above selection rules are exactly reversed.  [Pg.153]

These predictions involve some assumptions and approximations when applied in a generalised form. Thus symmetry is lacking in most reactants in cycloadditions, either because of different substitution at identical atoms (for instance vinyl derivatives instead of ethylene) or because different atoms are present as reactions centers (as in most 1.3-dipoles). In the former case the substance of the previous considerations should be unaltered , but in the latter case the selection rules (e.g. derived for the allyl anion taken as model of 1,3-dipole) may be less stringent when applied only on the basis of analogy. [Pg.153]

The largest body of data on cycloadditions concerns thermal processes allowed by the selection rules differences of opinion about concerted or two-step pathways for Diels-Alder reactions and for 1,3-cycloadditions cannot be settled by virtue of the rules. [Pg.153]

A more interesting field is that of the thermal 1,2-cycloadditions here concerted processes are forbidden, and experimental results can be compared with this prediction. A discrepancy arises in the case of keteiies, as there is considerable evidence in favour of a concerted mechanism for their thermal 1,2-cycloadditions (Section 6.1). However, it is possible to envisage the intervention of the perpendicular Tr-system of the C=0 bond of ketene, in such a way as to surmount the steric difficulties of an orthogonal approach of the reactants, required by a cis-trans (or supra,antara) cycloaddition the latter is symmetry-allowed as a thermal process when it is w + n = 4. [Pg.153]

The aim was to derive an expression for the instrument signal in response to the evolution of heat from a sample as represented by dh/dt. The sample and its crucible were considered as one with a total heat [Pg.65]

Thus the heat evolution from the sample is given by the instrument signal measured from zero (term i), a heat capacity displacement (term ii) and a third term which includes the product RC. This product has units of time so that term iii represents a thermal lag. Included in the publication was a recipe for obtaining dh/dt from the experimental curve by making allowance for thermal lag. For inert samples dh/dt = 0 and the displacement (term ii) provides a route to the determination of heat capacity. [Pg.66]

The model serves to focus attention on the need to reduce thermal lag as much as possible. Although the contribution to thermal lag from the instrument is fixed by the nature of its design the practitioner has some control over the contribution from the sample and crucible. For example, the use of small samples and slow heating or cooling rates, good contact between the sample and crucible and between the crucible and the temperature sensor will all reduce thermal gradients. [Pg.66]

Gray also discussed the shape of the leading edge of the peak for a melting transition. [Pg.66]

MTDSC represented something of a revolution in thermal analysis with an impact which has been compared to that of the original introduction of power compensation DSC. Numerous publications have appeared devoted to the complexity of the theory and the data manipulation techniques needed before useful information can be obtained. Fortunately all the hard work is done by the instrument software. Rather like conventional DSC, useful information can be obtained without recourse to the detailed theory. [Pg.67]

Potential Energy Hypersurfsoes.—So far in this chapter the emphasis has been on how one describes the results of reactive encounters between species in selected quantum states. Now it is time to examine what the fundamental factors are that control the collision dynamics, and therefore lead to different detailed results. This discussion will be based on the foundation of the Born-Oppenheimer assumption that is, that the motions of the nuclei during a collision are determined at all (or [Pg.18]

For oiu representative system of three atoms, the nuclear framework is defined by three intmiuclear distances and the potential energy can be written as F(r, fc )- For a given potential, the result of an individual collision (or, in quantum mechanics, the probabilities of various allowed results) depends on parametos such as the relative translational energy, impact parameter, etc., that specify the situation at the start of that collision. It is ibtform of the potential hypersurface, e.g. bo ca) distinguishes one molecular system from another and [Pg.19]

AB and, in some cases, ABC are chemically bound. In each of these four cases, as A approaches BC, r c tends to increase. The reverse is true for surface 3(a), where the dominant forces are repulsive. Since A repels B, the atom doser to it, more strongly than C, BC is compressed as A approaches. [Pg.19]

Figiire 3 Potential surfaces representing different types of molecular interaction (a)potential between a diatomic molecule BC and inart atom A as a function ofr c and x, the separation of A from the centre of mass ofBC (b) potential for a thermoneutral atom-transfer reaction with A= C so the barrier is symmetrically located (c) potential for an exothermic reaction A + BC - AB + C with only a low barrier to reaction (d) here ABC. as well as AB and BC, is bound and since A = C there is a symmetrically placed welV (e) again ABC is stable, but now A so the weW is not symmetrically placed. The blmk dots indicate the lowest points on the energy surfaces [Pg.19]

It may not only be the form of the intermolecular potential that is different when chemical reaction is posriUe. In addition, A -h BC may correlate with more than one electronic state. For collisions between He( 5o) and there is [Pg.20]

Hehre and Kahn have developed a model for the reaction of nucleophiles with a,p-unsaturated sulfoxides [64,124,125], that suggests that the product stereochemistries of many of these reactions are determined along the reaction coordinate on the basis of electrostatic interactions. They argue that the a,P- [Pg.190]

Extended Hixckel calculations are available on the coplanar endo-oriented W. J. Hehre, Accounts Chem. Res., 1976,9, 399. [Pg.144]

Wiberg and co-workershave analysed the p.e. spectra of C3—Cj cycloalkenes and methylenecycloalkenes utilizing MO energies etc., calculated with a 4-3IG basis set using the ab initio Gaussian-70 program. Conjugation effects in 1,2-diethyl-spiro[2,4]hepta-l,4,6-triene and related systems have been studied via their p.e. spectra n-cs interactions appear to be important in the former. [Pg.145]

Generally, the state of particle dispersion, which can be observed after a finite mixing time or at the end of an extrusion line, depends on the dispersion kinetics. It basically describes the rate at which the particles are transferred from the undispersed into dispersed state and is strongly related to the ongoing dispersion mechanisms. The occurrence of certain dispersion mechanisms is related to the nature of viscous flow as well as the mechanical stability of the agglomerates. [Pg.150]

To characterize the relationship between the external stress which is generated by the viscous flow of a liquid and the strength of agglomerates the dimensionless fragmentation number Fa (Eq. 5.3) or similar quantities are commonly used [33]. The product of the viscosity rj and the shear rate 7 in the numerator simply reflects the shear stress Tg in the case of simple shear. The denominator c% is the maximum strength of the agglomerates. [Pg.150]

Although real MWCNTs exhibit strong deviations from this simple model (inhomo-geneity, anisotropy) as well as the fracture surface is not necessarily even, two important statements can be derived. The agglomerate strength increases with  [Pg.152]

High values of the SME can be considered either as long mixing at low shear level or short mixing at high shear level. Thus, the dispersion degree should increase with the SME. [Pg.153]

The rates of chemical reactions are highly dependent on temperature. Temperature affects the rate constant of a reaction but not the order of the reaction. Classic thermodynamic arguments are used to derive an expression for the relationship between the reaction rate and temperature. [Pg.14]

The molar standard-state free-energy change of a reaction (AG°) is a function of the equilibrium constant K) and is related to changes in the molar standard-state enthalpy (AH°) and entropy (A5°), as described by the Gibbs-Helmholtz equation  [Pg.14]

Rearrangement of Eq. (1.46) yields the well-known van t Hoff equation  [Pg.15]

If the heat capacities of reactants and products are the same (i.e., ACp = 0) A5° and AH° are independent of temperature. Subject to the condition that the difference in the heat capacities between reactants and products is zero, differentiation of Eq. (1.47) with respect to temperature yields a more familiar form of the van t Hoff equation  [Pg.15]

For an endothermic reaction, AH° is positive, whereas for an exothermic reaction, AH° is negative. The van t Hoff equation predicts that the AH° of a reaction defines the effect of temperature on the equilibrium constant. For an endothermic reaction, K increases as T increases for an exothermic reaction, K decreases as T increases. These predictions are in agreement with Le Chatelier s principle, which states that increasing the temperature of an equilibrium reaction mixture causes the reaction to proceed in the direction that absorbs heat. The van t Hoff equation is used for the determination of the AH° of a reaction by plotting InTT against /T. The slope of the resulting line corresponds to —AH°/R (Fig. 1.10). It is also possible to determine the AS° of the reaction from the y-intercept, which corresponds to AS°/R. It is important to reiterate that this treatment applies only for cases where the heat capacities of the reactants and products are equal and temperature independent. [Pg.15]

Since this section is intended to investigate the optical properties of conducting polymers, it is relevant to review some basic optical properties of simple solids. Therefore, this section starts with a rather elementary treatment of the optical constants. The optical constants of solids provide information on their electronic and vibronic structure since the electromagnetic field of the light wave interacts with all fixed and mobile charges [1171,1172]. For a simple solid (a homogeneous, isotropic, and linear medium that is local in its response), the response of the system to the field is characterized by a complex dielectric function, e(o)), given as [Pg.63]

Introducing a complex refractive index, N = n + Ik, e(to) (= N ) is related to the reflective index, n, and the absorption index, , by the relations [Pg.63]

Due to the linear response of simple solids and as a result of causality [1171], ei( ) and s2( o) are connected by the Kramers-Kronig relation. Thus, if one knows either the real or the imaginary part of the optical constants for all frequencies, one can evaluate the other numerically. [Pg.63]

Such optical constants are connected with the experimentally determined absorption coefficient, a( a), and reflectivity, R(w), through the relations [Pg.63]

Therefore, having determined both R(to) and o(w), Eqs. (4.3) and (4.4) serve to obtain the refractive and the absorption indices n and k, as well as the complex dielectric function. Alternatively, if R(b ) can be measured over a sufficiently large spectral range, a Kramers-Kronig analysis also allows computations of a series of optical constants. In these circumstances, reflectivity measurements alone suffice in obtaining the dielectric function. [Pg.63]

The bulk (Young s modulus) of a quasi-one-dimensional polymer chain is given by  [Pg.374]

For a two-dimensional polymeric system, one can define the shear modulus [Pg.375]

An ab initio program has been developed in Erlangen for computing the band structure of a two-dimensional system with an arbitrary number [Pg.375]

10 Magnetic, Electrical, and Mechanical Properties of Polymers [Pg.376]

In the tunneling model [4] the TLS was described by two parameters (Fig. 5.2), the asymmetry parameter A and the overlap parameter A, which contains the barrier height, the distance of the two minima, and the mass of the tunneling particle. They are related with the total energy splitting E of the two levels and the tunneling matrix element Ao by the relations [Pg.71]

It is convenient, however, to use experimentally accessible quantities as variables, i. e. the energy E and a dimensionless relaxation rate R, which can be defined as = rtr = The transformation to the new variables yields for the distribution function [25]  [Pg.72]

Avery important feature of this distribution is the fact that P E, R) is independent of E. In order to keep the total number of TLS finite, some cut-off value for i 0 has to be introduced [3], which is usually denoted by [Pg.72]

It was shown in Ref. [15] that for optical transitions in glasses the TLS dynamics results in spectral diffusion, which shows up in the experiment as a time and temperature-dependent Lorentzian line broadening. The width of this Lorentzian line must be calculated by averaging over the distribution of energies and relaxation rates P E, R). It can be written as  [Pg.72]

Equation 5 represents the theoretical prediction of the tunneling model for the time and temperature-dependent broadening of spectral holes. This result, however, is the result of a particular form of the density of tunneling states P E, R), which is based on the a priori assumption of Eq. 2. A uniform density of states in A is a physically reasonable choice the independence of 1, however, is difficult to justify, since k consists of several parameters [28]. The temperature dependence of spectral diffusion is dominated by A the time evolution stems mainly from k. Therefore, these two predictions from Eq. 5 do not have the same validity. In our experiments we have investigated time and temperature dependence separately. [Pg.72]

Cebe [1,2] has reviewed current trends in the thermal testing of polymers. Apparatus for TGA is discussed in Appendix 1. [Pg.37]

The lifetime or shelf life of a polymer can be estimated from the kinetic data. Ozawa [3] observed that the activation energy of a thermal event could be determined from a series of thermogravimetric runs performed at different heating rates [4-8]. As the heating rate increased, the thermogravimetric changes occurred at higher temperatures. The measurement of lifetime is discussed in more detail in Section 2.2.8. [Pg.37]

TGA has been used to study a wide range of polymer characteristics including  [Pg.39]

Weight loss measurements and water or volatile contents Chemical composition [Pg.39]

Thermal stability including the effect of various factors such as crystallinity, molecular weight, orientation and tacticity, substitution of hydrogen atoms, grafting, co-polymerisation and effect of additives [Pg.39]

It is the objective of this section to calculate quantities of amorphous solid contained in an ideal potassium Kurrofs salt system in which / , the M2O-P2O5 ratio of a total system, is less than unity. [Pg.58]

It is known that at least one crystalline phase, [KPOal/i, is found in systems with ratios 1 K2O/P2O5 0.5. Only one crystalline phase can be detected by X-ray analyses. [Pg.58]

All attempts to form crystals in ultraphosphate systems with K2O-P2O5 ratios of 0.5 or less have been unsuccessful. Thermal analyses reveal an endothermic region extending from about 200 °C to the eutectic temperature at 450 °C. This amorphous region becomes more and more pronounced as M2O-P2O5 ratios are decreased to 0.5, where the total system is amorphous. [Pg.58]

No potassium ultraphosphates in the composition range 1 K2O/P2O5 0.5 are crystalline. [Pg.58]

All ultraphosphate systems considered here have a K2O-P2O5 mole ratio, such that I R 0.5. [Pg.58]

Wetting may be quantitatively defined by reference to a liquid drop resting on a solid surface as shown in Fig. 2.1. The tensions at the three-phase contact point are indicated such that Iv is the liquid/vapour point, si is the solid/liquid point and sv is the solid/vapour point. The Young equation [3,4], relating these tensions to the equilibrium contact angle, 6, may be written as  [Pg.19]

The term ysv represents the surface free energy of the solid substrate resulting from adsorption of vapour from the liquid and may be considerably lower in [Pg.19]

Whene 0° the liquid is nonspreading, but when 0 = (f the liquid wets the solid completely and spontaneously spreads freely over the surface at a rate that depends upon such factors as the liquid viscosity and roughness of the solid surface, as discussed later. Thus for spontaneous wetting to occur  [Pg.20]

These criteria may also be expressed by defining a parameter termed the equilibrium spreading coefficient, S, where  [Pg.20]

a liquid will spread spontaneously and completely wet a solid surface when S 0. It is also possible, of course, to make a liquid spread across a solid surface even when 0 O°, but this requires the application of a pressure or a force to the liquid forcibly to spread it over the solid surface. [Pg.21]

The probability of absorption of a photon widi energy hv by a molecule per unit of time leading to a transition between a lower energy state n to higher state n is given by [1-3] [Pg.2]

The polarization vector of the photons does not affect the molecular wave fimctions. A quantity called electric transition dipole may, therefore, be defined [Pg.2]

Pq q has components along the x, y and z axes of the molecule-fixed Cartesian system. The directions of u , and need not coincide since molecules are randomly oriented. There is, therefore, an angle 0 between the vectors u and Pn n - Eq- (1-1) may then be rewritten as [Pg.2]

The transition probability associated with absorption of a photon with energy hv is then given by [Pg.3]

The quantity Bn n- = (8a3/3h2) n lpln )2 is the well known Einstein coefficient of absorption. Per unit radiation density it is equal to die transition probability. The Einstein coefficient depends on the molecular structure and may, eventually, be used to characteri2e molecular properties on the basis of experimentally determined intensities of the respective transitions. [Pg.3]

The main electromagnetic field enhancement is now considered to come from a geometrically defined localized plasmon resonance within metal particles such as produced by an ORC pretreatment in an electrochemical system. [Pg.270]

The possibility of a photon-assisted charge transfer SERS mechanism involving an electronic resonance between states of the metal and the molecule was first suggested by a quantum mechanical treatment from our laboratory and, independently, by other groups for several types of charge transfer mechanisms.This theory, which was further developed,predicts a background continuum, which is observed experimentally. Subsequent [Pg.271]

FIGURE 3. Relative Raman intensity versus potential. (A) 0.05 M 2-methylpyridine in 0.1 M KCl for the 1008 cm band. (B) 0.05 M imidazole in 0.1 M KCl for the 1163 cm band. Scan rate 20 mV s Lower curves have excitation at 488 nm and upper curves have excitation at 600 nm. [Pg.272]


Hush N S 1967 Intervalence-transfer absorption. Part 2. Theoretical considerations and spectroscopic data Prog. inorg. Chem. 8 391... [Pg.2995]

IT. Total Molecular Wave Functdon TIT. Group Theoretical Considerations TV. Permutational Symmetry of Total Wave Function V. Permutational Symmetry of Nuclear Spin Function VT. Permutational Symmetry of Electronic Wave Function VIT. Permutational Symmetry of Rovibronic and Vibronic Wave Functions VIIT. Permutational Symmetry of Rotational Wave Function IX. Permutational Symmetry of Vibrational Wave Function X. Case Studies Lis and Other Systems... [Pg.551]

The choice of solvent cannot usually be made on the basis of theoretical considerations alone (see below), but must be experimentally determined, if no information is already available. About 0 -1 g. of the powdered substance is placed in a small test-tube (75 X 11 or 110 X 12 mm.) and the solvent is added a drop at a time (best with a calibrated dropper. Fig. 11, 27, 1) with continuous shaking of the test-tube. After about 1 ml. of the solvent has been added, the mixture is heated to boiling, due precautions being taken if the solvent is inflammable. If the sample dissolves easily in 1 ml. of cold solvent or upon gentle warming, the solvent is unsuitable. If aU the solid does not dissolve, more 11,27,1. solvent is added in 0-5 ml. portions, and again heated to boiling after each addition. If 3 ml. of solvent is added and the substance... [Pg.124]

A comparison of the reactivity of the heterocycles, selenazoie, thiazole. and pyridine, was made by Ochiai (41), who used theoretical considerations to show that the degree of aromaticity was ... [Pg.239]

The approximate nature of the relationship in Equations (2.16) and (2.17) needs to be emphasized. Not only does the heat of adsorption q in the first layer vary, in general, with the coverage 0i, but theoretical considerations as well as analysis of experimental data suggest that the factor aiV2/ 2v, ( = ni. [Pg.44]

Although theoretical considerations still fall short of the goal of giving absolute values of M from Vj, they do suggest ways in which empirical calibrations can be extended beyond the stringent requirement of identical polymers under identical conditions being the only acceptable calibrations. [Pg.649]

Other correlations based partially on theoretical considerations but made to fit existing data also exist (71—75). A number of researchers have also attempted to separate from a by measuring the latter, sometimes in terms of the wetted area (76—78). Finally, a number of correlations for the mass transfer coefficient itself exist. These ate based on a mote fundamental theory of mass transfer in packed columns (79—82). Although certain predictions were verified by experimental evidence, these models often cannot serve as design basis because the equations contain the interfacial area as an independent variable. [Pg.37]

The concept of functionaUty and its relationship to polymer formation was first advanced by Carothers (15). Flory (16) gready expanded the theoretical consideration and mathematical treatment of polycondensation systems. Thus if a dibasic acid and a diol react to form a polyester, assumiag there is no possibihty of other side reactions to compHcate the issue, only linear polymer molecules are formed. When the reactants are present ia stoichiometric amouats, the average degree of polymerization, follows the equatioa ... [Pg.35]

Much progress has been made ia understanding how to create and use catalysts, but the design and preparation of practical catalysts stUl rehes on a substantial amount of art that is, the appHcation of known facts and iatuition to trial and error methods. General principles are described ia a number of texts (18—21). Very few completely new catalyst systems have been designed from first principles or completely theoretical considerations. New catalysts are much more likely to be discovered as a result of an adventitious observation than designed by iatent. [Pg.195]

Theoretical Formulation of the Separative Efficiency. The separative efficiency E of a countercurrent gas centrifuge maybe considered to be the product of four factors, all but one of which can be evaluated on the basis of theoretical considerations. In this formulation the separative efficiency is defined by... [Pg.94]

The common theme in the evolution of methods for property and parameter prediction is the development of equations, either theoretical or empirical, containing quantities that can be calculated from theoretical considerations or experimental data. Mathematical expressions for correlating thermodynamic data may take several forms. [Pg.232]

Application The theoretical considerations that have been expounded should be used only for order-of-magnitude estimates, since a number of extraneous factors may enter into actual performance. In actual instaUations rectified alternating current is em-... [Pg.1611]

The correlations used are based partly on theoretical consideration and partly on empirical observations. The basic filtration data are correlated by application of the classic cake-filtration equation, aided by various simplifying assumptions which are sufficiently valid for many (but not all) situations. Washing and drying correlations are of a more empirical nature but with strong experimental justification. If steam or thermal diying is being examined, additional correlations are required beyond those summarized below for such applications, it is advisable to consult an eqmpment manufacturer or refer to pubhshed technical papers for guidance. [Pg.1699]

Tests conducted to operate centrifugal pumps as hydrauhc turbines throughout the head-capacity-speed range show that a good centrifugal pump generally makes an efficient hydraulic turbine. From theoretical considerations it is possible to state that at the same speed... [Pg.2525]

There are already many publications that deal with various aspects of the use of herbal drugs and of the ideas about the ways in which they work some of these are listed in the accompanying bibliography [7 12]. LJnencumbered by theoretical considerations, indications belonging to certain ar-... [Pg.20]

Muller, V.M., Yushchenko, V.S. and Derjaguin, B.V., General theoretical consideration of... [Pg.215]

Due to the combining effects of hydrodynamic and physicochemical factors, the study of cake structure and resistance is extremely complex, and any mathematical description based on theoretical considerations is at best only descriptive. [Pg.76]


See other pages where Theoretical consideration is mentioned: [Pg.657]    [Pg.641]    [Pg.1265]    [Pg.1265]    [Pg.2848]    [Pg.560]    [Pg.2]    [Pg.15]    [Pg.592]    [Pg.231]    [Pg.30]    [Pg.467]    [Pg.348]    [Pg.360]    [Pg.204]    [Pg.352]    [Pg.474]    [Pg.76]    [Pg.206]    [Pg.221]    [Pg.47]    [Pg.48]    [Pg.1585]    [Pg.1611]    [Pg.1852]    [Pg.2368]    [Pg.573]    [Pg.167]    [Pg.432]    [Pg.828]    [Pg.287]    [Pg.335]   
See also in sourсe #XX -- [ Pg.115 , Pg.152 ]

See also in sourсe #XX -- [ Pg.65 ]

See also in sourсe #XX -- [ Pg.2 ]

See also in sourсe #XX -- [ Pg.53 ]

See also in sourсe #XX -- [ Pg.58 ]




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