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Experimental Result

Experimentally, there are some hints for the existence of finite-size HPE aggregates. [Pg.78]

Real proteins are built up both from hydrophobic and polar amino acid residues, some of the latter can be charged. Many of the conformational and collective properties of proteins are due to a complex interplay between short-range (hydrophobic) effects and long-range (Coulomb) interactions. Electrostatic effects can also determine some of the unique solution properties of globular proteins. We have already discussed the results of simulations [Pg.80]

Another method leading to nonaggregating copolymers may be connected with the molecular design of their monomeric units. We have discussed an extended variant of the HP model, the HA side-chain model [97], that explicitly takes into account the amphiphilic nature of hydrophilic segments. [Pg.81]

It is believed that, using this model and the methods of sequence design suitable for computer simulations, one can construct copolymers capable of forming nonaggregating heteropolymer globules, with the ultimate objective of learning how to manipulate the polymer chemistry and system conditions in order to preclude the aggregation processes. [Pg.81]

Although we are primarily interested in the intermolecular effects, we will first characterize the behavior of single amphiphilic copolymers in a selective solvent. [Pg.81]

Results for bench-scale flow-reversal units operated in Russia (Boreskov et al., 1982 Matros, 1989) and China (Wu et al., 1996 Xiao and Yuan, [Pg.230]

1996) have been published. The experimental system used by Xiao and Yuan (1996) appears in Fig. 11. The reactor was 32 mm (i.d.) X 1100 mm and was packed with a Type S101 potassium-promoted vanadia catalyst to a depth of 900 mm. Inert packing, 100 mm, was placed above and below the catalyst. Wu et al. (1996) used the same commercial catalyst but employed a 50 mm (i.d.) x 4000 mm reactor, about half full of catalyst. By contrast, Russian researchers used a 175 mm (i.d.) X 1300 mm reactor. Development of the temperature profile after a switch in the direction of flow is shown in Fig. 12 for stationary, reproducible operation of a 2 m deep converter bed (Wu et al., 1996). Results for different S02 concentrations, superficial [Pg.232]

Equations in Table IX are written per unit of bed volume (A )g is a time averaged, mean axial bed conductivity. Dt is a longitudinal diffusivity and A allows for particle to particle conductivity. Not all the terms in the model as given in the table are important. For example, Wu et al. (1995, 1996) and Xiao and Yuan (1996) neglect the accumulation and dispersion terms in Eq. (30) and the accumulation and conduction terms in Eq. (28). [Pg.234]

Because the term r(CA- T) is exponentially dependent on T and can be nonlinear as well, a numerical solution or piecewise linearization must be used. To simplify the numerical manipulations, equations in Table IX are normalized by f = zIL, r = utIL, and x = 1 - C,7(C,)0, where i is normally S02. y also is a normalized quantity. The Peclet numbers for mass and heat are written PeM = 2RpulD and PeH = 2/ pcpu/A, for a spherical particle. They are also written in terms of bed length as Bodenstein numbers. It is [Pg.234]

TABLE IX Model for a Packed-Bed Catalytic Reactor with Periodic Reversal of Flow Direction  [Pg.235]

Typical results of the quenching experiments, i.e. both overall and depolarized light intensities as well as temperature are reported in Fig. 16.6 as function of [Pg.336]

The DTA results do not fit with the results coming from optics signal. In particular, the end of the process seems anticipated in the quenching experiments. It can be due to many reasons. First of all, the DTA experiments [Pg.337]

Final phase composition (a -I- P) of sPS samples solidified in the apparatus described in this work at 5K/s 9 200°C are reported in Fig. 16.9. These were evaluated on the basis of X-ray diffraction characterization [33]. The data clearly show a reduction in the overall final crystallinity by effect of an increase of solidification pressure from 0 to 450 bar. At room pressure (Fig. 16.8) overall final crystallinity degree in the sohd samples gradually decreases with cooling rate, and a phase is predominant at 5 K/s. The effect of an increasing pressure [Pg.339]

An interesting connection between stability and kinetics may be also implied from the stability diagram of the sPS, as displayed in Fig. 16.10. The [Pg.340]

Stress-Induced Phase Transitions in Metallocene-Made Isotactic Polypropylene [Pg.345]

Using the experimental setup (Fig. 15) described in the last paragraph, the fluorescence intensity correlation function was measured for a single terrylene molecule in p-terphenyl over nine orders of magnitude in time by the authors group [27]. The experimental trace in Fig. 16 clearly displays the characteristic features of photon antibunching and photon bunching. The onset of Rabi oscillations is clearly visible, too. We now want to discuss separately these three effects for different systems and what can be learned from such measurements. [Pg.57]

Rabi oscillations. The expression for the correlation function at short times [Pg.58]

Besides the antibunching near t = 0, the above equation describes the Rabi oscillations at short times and contains via the dephasing rate F2, l/Ti and 1/T as damping terms. This equation demonstrates that under the valid assumption of constant T - which is usually satisfied in the temperature range between 1 and 10 K - the pure dephasing time Tj can be extracted from the damping of the Rabi oscillations. [Pg.58]

In Section 1.2.2.2 it was shown that the optical linewidth of a single terrylene molecule in p-terphenyl is broadened by librational mode induced pure optical dephasing (Tl-processes) when the temperature is increased. In Fig. 18, is [Pg.58]

By measuring the decay rate A in dependence on the exciting intensity, the ISC parameters k i and 31 can be obtained by fitting Eq. (16) to the data. At high [Pg.59]

As examples, experimental F(E) isotherms at = constant for Pb and T1 UPD in acidic perchlorate electrolyte on AgQikl) single crystal faces with Qtkl) = (111) and (100) are shown in Figs. 3.9 and 3.10, respectively [3.97, 3.105]. These isotherms were measured stepwise, waiting for equilibrium conditions according to polarization routines illustrated in Fig. 3.11 using the twin-electrode thin-layer technique (TTL) for Pb UPD and the flow-through thin-layer technique (FTTL) for T1 UPD. [Pg.58]

Both thin-layer techniques were developed by Schmidt, Siegenthaler et al. [3.55, 3.67, 3.68] and allow an independent and precise measurement of q(E,p) and iXE.fi) isotherms. From the q-T plot, the electrosorption valency can be directly determined as illustrated in Fig. 3.12 [3.97, 3.105]. The electrosorption valency was found to be Y = z m both UPD systems indicating the absence of cosorption and competitive sorption processes in the systems studied. [Pg.59]

At this point, it should be mentioned that experimental TXE, ) isotherms obtained by electrochemical measurements provide only integral information on the thermodynamic properties of Me UPD overlayers. Therefore, the interpretation of IXE,m) isotherms without any direct structural information is relatively uncertain. [Pg.62]

Experimental Results.—The data of Kwart, Broadbent, and Bartlett shown in Table XVI and Fig. 20 for the photoinitiated polymerization of vinyl acetate at 25°C illustrate the method. The initiation rate Ri = 2flabs for steady illumination was first established as a function of the relative incident light intensity /o.rez and of the concentration Cs of the photosensitizer, di- -butyl peroxide. The inhibition method was used, duroquinone being the inhibitor it had previously been shown to act efficiently down to very low concentrations. Thus, the proportionality constant between Ri and the product cJo.rez was determined. Two sets of polymerization rate measure- [Pg.155]

The rate of growth of an individual vinyl acetate radical, in [Pg.157]

The propagation rate constants for the seven monomers represented in Table XVII vary over a range of nearly one-hundred-fold. Since both reactants, radical and monomer, differ in each instance, no con- [Pg.157]

Methyl methacrylate s Methyl acrylate i Butyl acrylate 88 Methacrylonitrile89 Butadiene 99 Isoprene O  [Pg.158]

Propagation constants for butadiene and isoprene were determined from rate of polymerization per particle in emulsion polymerization. [Pg.158]

Experimental results for the standard SCR reaction study are presented in Fig. 13.3. A substantial performance degradation is observed for the low length— high washcoat loading samples. The difference in NOj conversions is observed above 250 °C for Cu-zeolites and 350 °C for Fe-zeolites, indicating that diffusion limitations are present. [Pg.398]

Similar experimental procedure was carried out for the NO-NO2-NH3 reacting system. The presence of N02/NO c ratio of 50 % in the feed stream greatly enhances the NO conversion efficiency as the fast SCR is the governing reaction in the system. Higher space velocities were necessary to achieve lower conversions and to make the observation of mass transfer limitations possible. The experimental results obtained for the Fe-zeolite catalysts are shown in Fig. 13.4. Washcoat diffusion limitations are present throughout the whole temperature range with the short monolith sample constantly achieving lower NO conversions. [Pg.398]

The kinetic parameters of the ID + ID model were calibrated to fit the experimental results produced by Metkar et al. [40]. Thermophysical properties and microstructural data for the zeolite washcoat and the substrate were obtained from the literature. In Fig. 13.5a simulated and experimental results are presented for the pair of FeZ-XX catalysts. An overall good agreement is observed, with the [Pg.398]

Washcoat tortuosity t[-] is an important empirical parameter in the computation of the effective diffiisivity of species inside the washcoat pores (13.15). A parametric analysis of washcoat tortuosity, shown in Fig. 13.5b, resulted in a value of T = 2.0 as the best value to reflect the extent of the internal diffusion impact on de-NOjc activity. [Pg.399]

We consider first the results on p-GaP. The impedance data for p-GaP has been a fruitful source of controversy, though not of comprehension. If a sample of p-GaP is held at a negative potential for a considerable period and then slowly ramped towards positive potentials, the a.c. impedance data cannot be analysed within the framework of the two-component model. Attempts to do so lead to Mott-Schottky plots whose slopes and intercepts are both frequency-dependent as shown in Fig. 25. If the data are analysed according to the more complex five-component equivalent circuit shown above, then a much better fit is obtained for the potential region more than about 0.6 V negative of the predicted flat-band potential. In this region, the Mott-Schottky plot is linear with a slope that corresponds reasonably well [Pg.413]

Such a detailed qualitative fit is quite remarkable and, taken with the a.c. [Pg.416]

Further careful examination of Fig. 27(c) reveals that, however, for poten- [Pg.416]

It might reasonably be asked what the origin of this behaviour pattern is and Fig. 28 shows the variation in ellipticity of a sample of p-GaP measured [Pg.419]

The E0 transition in GaAs is the simplest single transition that can be investigated within the III/V materials and a detailed quantitative fit has been attempted to the data of Fig. 29. A careful analysis of these data lead to the fit shown in Fig. 17 and it is clear that all the features of the experimental spectrum can be reproduced with some precision provided that the manufacturer s acceptor density be taken as the basis for the analysis. By comparing the changes in the Franz-Keldysh oscillation near 820 nm with those calculated using the intermediate field model with a presumed parabolic decay of potential inside the semiconductor depletion layer, it is found that some 70 10% of the potential is dropped inside the depletion layer of this n-type material, as can be seen in Fig. 30, and there is no evidence for the phenomenon described in the previous paragraph whereby the band [Pg.420]

Thiel and Madey s review (1987) gives a good overview of the experimental studies on water dissociation at surfaces. Most of these studies have been performed on powders which become hydroxylated more easily than planar surfaces. This effect is assigned to the high density of defects on powders. It is confirmed by several studies of water dissociation on planar surfaces with low densities of steps (Brookes et al, 1987 Onishi et al, 1987 Sanders et al, 1994). [Pg.181]

Unlike rutile, the stoichiometric SrTiO3 001 faces do not dissociate water at room temperature. The same is true for the tungsten NaojWOs and lead PbO oxides. However, on lead oxide, isolated oxygen atoms may be dissociation centres. On the (110) face of casserite Sn02, the strongest dissociation of water molecules takes place for a low density of vacancies (Gercher and Cox, 1995). [Pg.182]

On AI2O3 surfaces, a coexistence of several types of OH groups and water molecules has been found (Coustet and Jupille, 1994a Frederick et al, 1991b). On the reconstructed (100) face of Cu02, terminated with copper atoms, hydroxyl groups and water molecules are detected at 110 K, while only dissociative adsorption takes place at 300 K (Cox and Schulz, 1991). Thanks to adsorption isotherm measurements and infra-red absorption, hydroxyl groups have been identified on BeO(lOlO) (Miyazaki et al, 1985). On thin nickel oxide films, dissociation of water may occur on the polar 111 faces, but it depends upon the oxide thickness. [Pg.182]

More recently, photoemission (Onishi et al, 1987) and HREELS (Shido et al, 1989 Wu et al, 1991a Coustet and Jupille, 1994b) experiments have been performed on MgO. OH groups have been identified by photoemission on the 001 face and on the faceted 111 face, and their oxygen Is levels have been shown to be shifted towards larger binding energies, by 2.5 eV with respect to the bulk. [Pg.182]

Infra-red absorption and HREELS give access to the values of the OH stretching frequencies. When water, acids or bases are dissociated on a surface, several types of OH groups are formed. Some result from the [Pg.182]

The remainder of this chapter is devoted to a discussion of some of the results obtained from studies of negative-ion-neutral reactions. No attempt is made to include extensive discussion either of associative detachment processes (see Chapter 8) or of those many negative-ion reactions which have been studied only at relatively high energies, i.e., above a few hundred eV. Two-body rate coefficients here are invariably given in units of cm sec and cross sections in units of cm. Energies refer to kinetic energies of the reactant ion in the laboratory system, unless otherwise stated. [Pg.83]

The experimental aspect will be presented first, to emphasize the dearth of such results. We can put polynitrogens into four classes neutral molecules, extended-molecular allotropes, isolable ions, and ephemeral ions mainly of mass-spectrometric interest. This fourth class will not be discussed. [Pg.142]

Neutral molecules are the polynitrogen species of main interest because they represent pure polymerized nitrogen without the esthetic distraction of a counterion, because they have been the most difficult to realize experimentally, and because being pure nitrogen they are in principle the best candidates for high-energy-density materials. Closed-shell species would seem to be of particular interest, because most stable molecules fall into this class, but radicals and even-electron open-shell molecules will also be mentioned where appropriate. We will consider N3, N4, N5, Ne, N7, Ng, and larger molecules . [Pg.142]

The simplest neutral polynitrogen, the N3 radical (azide radical), has been generated as a fleeting molecule by flash photolysis of HN3 (hydrazoic acid) [1] and by reaction of HN3 with fluorine atoms [2], Being a simple free radical, there appears to be no question of its isolation as a stable substance. [Pg.142]

Neutral N5 is perforce a radical and so one immediately suspects that it will not be a reasonably stable species, and in fact there do not appear to be any reports of attempts to synthesize or detect this molecule. [Pg.143]

Neutral Ny is (like N5) a radical and so is likewise not expected to be reasonably stable. In an experiment of some relevance to Ny, laser-ablated scandium atoms were codeposited with argon/nitrogen at 10 K (the purpose was to study scandium nitride species) [16]. The reported IR spectra gave no indicahon of the presence of a compound with an Ny ring coordinated to scandium, a compound which has been predicted by computational methods to have a fair chance of existing [17]. [Pg.143]

FIGURE 5.28 (a) Radius of the spreading front vs. time. Points correspond to six different experimental runs, (b) Radius of the dry spot vs. time. Points correspond to six different experimental runs. [Pg.474]

In conclusion, the radius of the dry spot moves with the speed predicted by the theory, whereas the front edge of the moving part of the layer proceeds slower than theoretically predicted during the second spreading stage. The discrepancy may be due to one or both of the following reasons  [Pg.475]

Our assumption that the surfactant used is insoluble during the whole duration of the experiment may not be fuUy correct. Unfortunately, we have been unable to estimate the desorption time, T. If that time is reached during our experiments, dissolution of surfactant in the bulk may be significant at the higher front edge. [Pg.475]

Derivation of Governing Equations forTime Evolution of Both Film Thickness and Surfactant Surface Concentration [Pg.475]

At e 1, as we already noticed in Chapter 3, the Navier-Stokes equations reduces [Pg.475]

It will be convenient to have most of the experimental results collected under the one heading, although the presentation of some data will be delayed until the following section. [Pg.4]

The pressure dependence of the atomization rate varies with the temperature of the metal and the pressme of the gas. For a given [Pg.4]

If the temperature of the metal is sufficiently low, the pressure dependence of the atomization rate is accurately half order over a wide range of pressure, as can be seen from Fig. 1, which refers to the hydrogen-tungsten system (ii) equivalent results have been obtained for the [Pg.5]

5 MODELING HYDROCRACKING OF MAYA CRUDE OIL 11.5.1 Experimental Results [Pg.425]

Modeling of Processes and Reactors for Upgrading of Heavy Petroleum [Pg.426]

All of the above concepts must be addressed in interpreting the experimental results on the various measures of the equilibrium structures of polyelectrolyte chains in dilute solutions. [Pg.90]

Dependence of Rg (nm) of Et - PVP - Br on Confour Length and Saif Concenfrafion of NaBr [Pg.91]

Source Beer, M. et al., Macromolecules, 30, 8375, 1997. With permission. TABLE 4.2 [Pg.91]

The experimental data in Table 4.2 show that the specificity of the counterions plays a significant role in determining the polymer size. The [Pg.91]

This chapter is organized as follows. Section 11.1 presents an overview of the synthesized ASIC chip designs. Section 11.2 describes the synthesis results for several benchmark designs. [Pg.253]

At this date there is not a universally accepted model for electron and hole conduction in a-Si H. The theory is still not adequate to unequivocally fit the experimental Hall-effect data to the various models that have been proposed. Some of the theoretical difficulties that remain have been discussed by Mott (1978). It should be pointed out that anomalous behavior of the Hall effect, both in sign and in temperature dependence, is not necessarily limited to noncrystalline semiconductors but can occur whenever there is strong localization of the carriers, for example in impurity bands and inversion layers at low temperature (T 10 K). Despite these complications, the measurements of jUn combined wdth other transport parameters have shed much light on the states involved in the conduction process. [Pg.200]

The first measurements of on materials doped with phosphorus and boron were performed by LeComber et al. (1977) and are shown in Fig. 3. The most important result is that the sign of is reversed for both electrons [Pg.200]

Another question on which measurements of have yielded valuable information is that of which states are involved in electron conduction for undoped a-Si H. Based on an analysis of conduction and drift mobility in [Pg.201]

Determining the length of the polymer product is of key importance for understanding the polymerization process and received considerable attention ever since the reaction was discovered. On the experimental side direct determination is impeded by the insolubility of most polydiacetylenes — exceptions will be mentioned below — which precludes application of standard methods for measuring the molecular weight. [Pg.9]

Of particular interest are changes in the chain length occurring in connection with the autocatalytic reaction acceleration in TS-6. Numerous thermal polymerization studies showed that the activation energy is EJl = 1.00 + 0.02 eV, independent of conversion. Consequently the autocatalytic reaction enhancement cannot be the result of an increase of the Boltzmann factor. Instead, an increase in the number of monomers consumed per primary chain initiation event has been postulated. Experimentally n(X = 0.5)/n(X = 0) = 200 is found [Pg.9]

An early estimate, based upon the position of the optical absorption of TS-polymer at low conversion gave n(X = 0) 24 repeat units Although the conclusiveness of the procedure to derive this number is questionable — for n 10 the position of the lowest absorption band of the polymer backbone is almost independent of n yet sensitive to chain expansion, known to be important at low X — this number has turned out to be essentially correct. Analysing diffusive features in the X-ray diffraction pattern of partially polymerized TS crystals Albouy et al. recently [Pg.9]

There is, however, serious doubt that 4 pm is the kinetic length of an individual chain. Consider a monomer crystal that contains a fraction Xo of short chains consisting of no repeat units. The average number of monomers enclosed between the ends of two polymer chains in a row and available for subsequent photopolymerization is  [Pg.11]

Inserting no = 30, Xo = 0.1 gives n = 270. n should be an upper hmit for the average chain length in the autocatalytic reaction regime, if for reasons to be discussed below any further limitation of the kinetic chain length is suspended and if dead chain ends are not revived by recombination with a running chain. [Pg.11]

Final residue trial reports should include key information for field trials, analysis method, and experimental results. [Pg.333]

The protocol of field trials should include the following information  [Pg.333]

1) Field application rate (or concentration) of pesticide, application method, timing, and equipment. [Pg.333]

2) Plot size of the field (or number of crops), treatment intervals and number of applications, and PHI. [Pg.333]

3) pH value of soil in the experiment area, soil nature, organic matter content, climate conditions, and cultivation system. [Pg.333]

Relatively few small angle neutron scattering studies have been performed on block copolymers in comparison to those on homopolymers, the majority of the published work is concerned with the solid state with little work reported on block copolymer solutions. Results on isotopic block copolymers, e.g. polystyrene molecules with [Pg.11]

The Bueche-Mullins method has been applied in the separation of the modulus contributions of crosslinks and entanglements in several elastomers. A front factor of g = 1 was then used to determine Me. The Langley method has also been applied in a few cases, resulting in values of both g and Me. These works are summarized below results are collected in Table 7.2. [Pg.114]

Vander Hoff and Buchler (277) found Me= 13000 for natural rubber by applying the Bueche-Mullins analysis to the data of Bristow (288). Examination of the natural rubber results published some years ago by Flory et al. (289) yields Me% 15000. The data of Mullins (290) provides a value of 10000 for 1,4 polyisoprene if the total initial modulus is used in the analysis (Mullins reported Me = 16000 by examining the effects of primary molecular weight and extent of cure on C, alone the initial modulus G is C1 + C2 and C2 0.6 Cx in the samples examined). [Pg.114]

Ferry and co-workers (295) have obtained a value Me = 13000 for 1,2 polybutadiene by a new method which involves crosslinking the polymer in a strained state. The initial extension of the uncrosslinked sample, the recovery after [Pg.114]

Polymer Mt from the Me from Value of Method Investigators [Pg.115]

4 Polyisoprene 5800 13000 Bueche-Mullins Vander Hoff and Buchler (277) [Pg.115]

As already some excellent reviews have appeared (e. g. Nafie, 1984 Stephens and Lowe, 1985), emphasis is placed on the achievements of the last five years. Freedman et al. (1991) give a detailed analysis of the VCD spectra of (S, S)-[2,3- Fl2]oxirane both in solution and in the gaseous phase. The analysis is based on an ah initio calculation using the 4-2IG basis set and the experimental geometry. [Pg.557]

Eggiman et al. (1991) measured the VCD spectrum of 6,8-dioxabicyclo[3.2.1Joctane as solution in CCI4 and CS2 from 800 to 1500 cm. They compare the experimental absorption and VCD spectra with calculations using the FPC, CF and APT models. They found moderate agreement. [Pg.557]

The measurement of vibrational circular dichroism was confined to the region below 15 pm resulting from the transmittance characteristics of the photoelastic modulator made from zink selenide (ZnSe). This was changed by the employment of a photoelastic modulator made from cadmium telluride (CdTe) with sufficient transparency down to about 300 cm.  [Pg.557]

The spectrum of (-)-a-pinene as a 50 pm film of neat liquid using a Bomem spectrometer with a polarizing interferometer attachment is a composite of 60 000 VCD scans and 12 000 transmission scans and took 19.5 hours to be measured. A spectrum with comparable signal to noise ratio is shown in Fig. 6.3-9. This was measured in our laboratory with a PEM-based VCD spectrometer and is a composite of only 5000 scans (five blocks of 1024 scans each). The noise estimate shown as the upper trace is the difference between two 5000 scan VCD spectra. [Pg.558]

The synthesis, normal mode analysis and the comparison of experimental and calculated VCD spectra report Malon et al. (1992) on dideuteriobutyrolactone. For the calculations they use the 6-3IG basis set. The spectra of Oxiran and its deuterated analogues have been calculated by Duller and Rauk (1989) and compared to the results of unpublished measurements of Spenzer et al. [Pg.558]

The sawing rate remains proportional to Ftot. Below certain threshold values, which depend on the viscosity, the sawing rates are reduced considerably. In the next section the main dependencies will be compared with experimental results. [Pg.470]

The space between the rotating plate and the rotating crystal is filled with slurry and free-floating abrasive particles. The crystal is pushed downwards in the experimental setup. [Pg.472]

Particles with a diameter I greater than the slurry film thickness ho are in contact both with the crystal and the workpiece surface. Their number m can be calculated in the same way as before from Eq. (18.19). Therefore, one obtains the same equation (Eq. (18.21)) for the material-removal rate. However, the number of particles that are in direct contact, the effective total force Ff, and thus the material-removal rate will be different from the wire-sawing case. [Pg.472]

The rolling-indenting model of free-floating particles in the slurry forms the basis of the wire-sawing process. Combined with the fracture-mechanical processes of individual particles indenting into the crystal surface one can derive a [Pg.472]

If the main load of the wire is carried by the film, only a small force is exerted on the interacting particles, resulting in a low material-removal rate. If the film thickness decreases the large particles begin to carry the main load and abrasive action begins. The slurry is then mainly responsible for the transport of the particles. If the film thickness decreases further transport becomes more difficult and dry friction and wire rupture may occur. [Pg.473]

About 30 years later Kricheldorf and Schwarz [45] studied the addition of tetra(ethylene glycol), TEG, onto HMDI in benzene and in bulk at 60 °C. At that time MALDI-TOF mass spectrometry was available and the author observed that with 1/1 feed ratios a considerable fraction of linear chains having two TEG end groups existed in the reaction mixture indicating a consumption of HMDI by side reactions, such as the formation of allophanate groups. An excess of 4—7 mol % of HMDI was needed to transform all linear species into cycles. These results deviate from the comments of Stepto and Waywell, who concluded that a 1/1 feed ratio is [Pg.107]

Polycondensations in bulk were also conducted with other silylated diphenols [58, 59], for instance, with hydroquinone 4-hydroxybenzoate ((d) in Formula 7.2). These experiments had the purpose to elucidate, if end-to-end cyclization occurs even in the nematic phase. Liquid-crystalline phases are based on a more or less parallel alignment of the polymer chains, which is the most unfavorable conformation for ring closure. Nonetheless, cyclic oligo-, and polyesters were detected, and interestingly the even-membered rings prevailed largely in contrast to [Pg.108]

Further studies were devoted to syntheses of polyamides [60, 61] via KC polycondensations. The monomer combinations were selected so that polyamides having a moderate or good solubility in the reaction media were obtained, so that early precipitation of linear chains from the reaction mixture was prevented (e.g., (a) in Formula 7.3). From the best experiments spectra exclusively displaying mass peaks of cyclic polyamides up to 13 kDa were obtained. Similar results were found for soluble polyimides derived from the dianhydrides (b) and (c) (in Formula 7.3) and various aromatic diamines [62, 63]. [Pg.109]

Further interesting findings resulted from syntheses of aromatic poly(ether sulfone)s [64, 65]. The fraction of cycles increased at the expense of linear chains with increasing conversions. Due to the lower reactivity, 4,4 -dichlorodiphenyl sulfone yielded lower molar masses than 4,4 -difluorodiphenyl sulfone, with the consequence that the fraction of cycles was lower. Poly(ether sulfone)s derived from tert-butyl catechol ((d) in Formula 7.3) proved to be particularly well suited to MALDI-TOF mass spectrometry. The poly ether with the highest molar mass gave a spectmm showing mass peaks of cycles up to 20 kDa. After fractionation mass peaks of cyclic polyethers up to 27 kDa were achieved and no signals of linear chains were detectable. However, the fraction above 27 kDa certainly contained linear chains, because in a real experiment 100 % conversion without any side reaction cannot be achieved. The formation of cyclic polyethers in syntheses of poly(benzonitrile ether)s (e.g. (a) in Formula 7.4), of poly(pyridine ether)s ((b) in Formula 7.4) and of poly(ether ketone)s was also screened by MALDI-TOF mass spectrometry [66-68]. [Pg.110]

In previous sections, the set of infinite elementary reactions occurring in step-growth polymerization was shown to reduce kineticaUy to a single reaction involving functional groups. It was essential to assume the equal reactivity hypothesis in order to achieve this simplification. Thus, tests against various experimental results are needed to confirm the equal reactivity hypothesis. In this section, however, experimental results on several important commercial systems are presented, and we find that the simple model presented earher needs to be substantially extended to explain them. In fact, in several situations the equal reactivity hypothesis itself is inapplicable. [Pg.125]

In order to confirm the equal reactivity hypothesis, Flory originally studied the polymerization of adipic acid with decamethylene glycol in the absence of a strong acid [4,5]. The course of the polymerization was followed by titrating the carboxylic end group. Flory assumed that the carboxylic groups act as a catalylst, and he represented the polymerisations as [Pg.125]

In this experiment, conditions were maintained such that reaction (3.7.1) remained irreversible during the entire period of study. If the hydroxyl and the carboxylic acid groups are present in an equimolar ratio, Eq. (3.7.2) can be integrated to give [Pg.125]

If the initial concentration of the carboxyHc acid group is [—COOH]q, then its concentration at any time can be expressed as a function of the conversion, p, as follows  [Pg.125]

Similarly, for acid-catalyzed polymerization, instead of Eq. (3.7.6), d[COOH] [Pg.127]

The dimensionless curvature is used to preclude the influence of small thickness variations between specimens. [Pg.258]

The intramolecular orientations of the transition dipoles for the St and S2 bands of ethidium were determined from polarized fluorescence studies of [Pg.172]

When the internal motion is so rapid that it relaxes before significant relaxation by twisting and bending takes place, there exists a time domain in which 7 (t)s/n(oo)yet C (t) = 1.0, F (t)s 1.0, and the residual anisotropy is given by [Pg.174]

Although it is assumed in this and the preceding section that the reduction in residual amplitude is due entirely to internal Brownian motion of the dye in its binding site, other mechanisms of amplitude reduction are also possible. [Pg.175]

It is conceivable that the equilibrium orientation of the intercalated dye in its Sj excited state differs from that in its S0 ground state and that this is what is responsible for the rapid initial relaxation. If so, the rms amplitudes of internal Brownian motion estimated above would be upper limits to the actual values. [Pg.176]

The reported initial anisotropy(87) was r(0) = 0.39 0.01, which is within experimental uncertainty of the theoretical value 0.40. Evidently, there is no significant amplitude of faster motions. However, internal motions of the dye on a time scale much longer than 120 ns would not be detected in FPA experiments, as they would provide only an effectively static equilibrium distribution of dye orientations over the observation period. [Pg.176]

As already noted the strength of chemisorptive bonds can be varied in situ via electrochemical promotion. This is the essence of the NEMCA effect. Following initial studies of oxygen chemisorption on Ag at atmospheric pressure, using isothermal titration, which showed that negative potentials causes up to a six-fold decrease in the rate of 02 desorption,11 temperature programmed desorption (TPD) was first used to investigate NEMCA.29 [Pg.170]

Massive oxygen backspillover from the solid electrolyte onto the catalyst surface takes place under electrochemical promotion conditions. [Pg.172]

Increasing catalyst potential and work function leads to a pronounced increase in total oxygen coverage (which approaches unity even at elevated temperatures) and causes the appearance of new chemisorption states. At least two such states are created on Pt/YSZ (Fig. 4.43) A strongly bonded one which, as discussed in Chapter 5, acts as a sacrificial promoter during catalytic oxidations, and a weakly bonded one which is highly reactive and causes the observed dramatic increase in catalytic rate. [Pg.172]

These important conclusions are not limited to Pt/YSZ only. Similar is the behaviour of Ag/YSZ31,119 (Fig. 4.44) and Au/YSZ.119 In the last case actually gaseous oxygen adsorption is negligible.119 [Pg.172]

As discussed in detail in Chapter 5 this is not a coincidence. Similar is the behaviour of oxygen chemisorption on Ag31,119 and on Au119 and the Ed vs D slopes are -1 and -4 respectively. Furthermore such a linear decrease in Ed with L is in agreement with rigorous cluster quantum mechanical calculations.120,121 [Pg.174]

According to Eq. (2), the work function for a metal M is related to the potential of zero charge for the M/aqueous solution interface by [Pg.14]

For the sd metals (Au, Ag, and Cu) the situation is more complicated. Higher X is associated with lower heat of oxide [Pg.15]

The experimental data bearing on the question of the effect of different metals and different crystal orientations on the properties of the metal-electrolyte interface have been discussed by Hamelin et al.27 The results of capacitance measurements for seven sp metals (Ag, Au, Cu, Zn, Pb, Sn, and Bi) in aqueous electrolytes are reviewed. The potential of zero charge is derived from the maximum of the capacitance. Subtracting the diffuse-layer capacitance, one derives the inner-layer capacitance, which, when plotted against surface charge, shows a maximum close to qM = 0. This maximum, which is almost independent of crystal orientation, is explained in terms of the reorientation of water molecules adjacent to the metal surface. Interaction of different faces of metal with water, ions, and organic molecules inside the outer Helmholtz plane are discussed, as well as adsorption. [Pg.16]

For the metal in the interface, the surface potential of the electrolyte phase is nearly the same for all crystal orientations.29 Therefore, referring to Eq. (2), the potential of zero charge varies with the surface potential or the work funtion and is larger for the most densely packed faces. Correspondingly, atomic irregularities [Pg.16]

It may be noted that the statement made above—that the surface potential in the electrolyte phase does not depend on the orientation of the crystal face—is necessarily an assumption, as is the neglect of S s1- It is another example of separation of metal and electrolyte contributions to a property of the interface, which can only be done theoretically. In fact, a recent article29 has discussed the influence of the atomic structure of the metal surface for solid metals on the water dipoles of the compact layer. Different crystal faces can allow different degrees of interpenetration of species of the electrolyte and the metal surface layer. Nonuniformities in the directions parallel to the surface may be reflected in the results of capacitance measurements, as well as optical measurements. [Pg.17]

The trend shown toward increasing routing blocks demonstrates that the application of artificial evolution (i.e., a GA) to the problem of finding rules that can grow effective (though not optimal) digital circuits is a real technological possibility. [Pg.298]

The ALIS-based off-rate measurement method was applied to a proprietary series of Zap-70 Kinase inhibitors. First, an ACE50 experiment was conducted to demonstrate that the compounds bind the same site as the quench reagent staurospor-ine. As shown in Fig. 3.15, sigmoidal plots indicate that, with the exception of one compound, the ACE50 values were all very similar to one-another. Linear ratio plots of the same ACE50 data confirm that the compounds all bind isosteri-cally with respect to the quench reagent, a necessary prerequisite for effective competition. [Pg.147]

The mixture of these compounds at 0.5 xM per component was equilibrated with a 5 pM concentration of the protein target, then the reaction was quenched with excess staurosporine (100 pM) and analyzed using ALIS every 7 min. The measured protein-ligand complex MS responses were normalized and fit to the exponential decay function above, as shown in Fig. 3.16. The raw data fit the ex- [Pg.147]

3 ALIS An Affinity Selection-Mass Spectrometry System for the Discovery and Characterization [Pg.148]

ALIS-MS response data. Each curve (left to right) corresponds to the compounds listed in Table 3.1 (top to bottom). NGD-6367, from (A), is shown as a dashed line. For clarity, the raw data points are not shown in [Pg.148]

The ALIS quench method for dissociation rate measurement uses little protein and requires no biochemical assay for its implementation, yet the method readily yields quantitative values for the dissociation rates of the protein-ligand complexes. The technique can be used with pools of ligands to provide a quantitative rank ordering of the dissociation rates of all the components of the mixture. Since it is not necessary to know the exact concentrations of the ligands under study, the dissociation rate assessment can be performed using impure compounds, such as unpurified compound mixtures derived from combinatorial chemistry synthesis. The method does not require a foreknowledge of active protein concentration to measure and rank ligands based on their rates of dissociation. As such, the technique is self-contained and does not rely upon an external measure of protein activity as one of its input parameters. [Pg.150]

Eigure 4.2. The E dependence of the storage G (solid symbols) and loss G (open symbols) moduli of a mono-disperse silicon oil-in-water emulsion stabilized with SDS, with radius a = 0.53 jam, for three volume fractions from top to bottom (j = 77%, 60%, and 57%. The frequency is 1 rad/s the lines are visual guides. (Adapted from [10].) [Pg.130]

The frequency dependence of the moduli was measured by Mason et al. [7,8] and is shown in Fig. 4.3 for several values of . In all cases, there is a plateau in G ( y) at high 4 , this extends over the full four decades of explored frequency, while for the lower 4 , the plateau is no longer strictly independent on co but reduces to an inflection point at G. In contrast, for all 4 , G co) exhibits a shallow minimum, G . Mason et al. used G to characterize the elasticity and G to characterize the viscous loss. [Pg.130]

Rgure 4.4. The plateau storage modulus (small solid symbols) and the minimum of the loss modulus G (small open symbols) as a function of the effective oil volume fraction. a = 0.25 um (circles), a = 0.37 j,m (triangles), a = 0.53 um (squares), and a = 0.74 qm (diamonds). The large circles are the measured values for the osmotic pressure. All data are normalized by yint/a (Adapted from [10].) [Pg.131]

The rescaled data of G and G all fall onto single curves as shown in Fig. 4.4 G p rises by about four decades, as (peg increases from 60% to 85%. The scaling with Kint/a confirms that the origin of elasticity results from the storage of energy [Pg.131]

Absorption spectra. The absorption coefficient, a, also called the absorption spectrum if known as a function of frequency v, is obtained from a measurement of transmitted and incident intensities, /(v) and /o(v), of monochromatic light, according to [Pg.56]

Our main interest is the absorption which arises from complexes of interacting atoms and/or molecules, i.e., the absorption which exceeds the simple sum of the absorption spectra of the individual (non-interacting) atoms and molecules (where such monomer spectra exist). This excess absorption is of a supermolecular nature. It will be called interaction-induced, or briefly induced absorption. [Pg.56]

Spectroscopists have always known certain phenomena that are caused by collisions. A well-known example of such a process is the pressure broadening of allowed spectral lines. Pressure broadened lines are, however, not normally considered to be collision-induced, certainly not to that extent to which a specific line intensity may be understood in terms of an individual atomic or molecular dipole transition moment. The definition of collisional induction as we use it here implies a dipole component that arises from the interaction of two or more atoms or molecules, leading at high enough gas density to discernible spectral line intensities in excess of the sum of the absorption of the atoms/molecules of the complex. In other [Pg.56]

Collision-induced emission. Induced spectra are usually studied in absorption. However, emission spectra of supermolecular nature will also interest us here, for example, in connection with shock tube measurements and astrophysical studies (stellar and planetary atmospheres). [Pg.57]

About units. For our survey of measured spectra and the comparisons with theory that follow in Chapters 5 and 6, it is useful to remember that frequencies are often expressed in units of Hertz, or of cm-1, or in cycles per 2n seconds. In order to avoid confusion we shall distinguish the notations f,v=f /c, and co = 2nf, respectively, where c designates the speed of light in vacuum. Similarly, gas densities will be expressed as number densities, n, the number of particles per volume, or in units of amagat, q = n/Na, where Na is the number of particles per cubic centimeter of the gas under consideration for most gases of interest Na is about equal to Loschmidt s number, Na Nl = 2.686763 xlO19 cm-3 amagat-1, the particle density of an ideal gas at standard temperature and pressure. The values of fundamental constants are taken from [124], [Pg.57]

These cyclics can change the properties of the network in which they are trapped. Because they restrict to some extent the motions of the network chains, they should increase the modulus of an elastomer. Some small but possibly significant increases in low-deformation moduli have, in fact, been observed [192], Also, when PDMS cyclics are trapped in a thermoplastic material, they can act as a plasticizer that is in a sense intermediate to the usual external (dissolved) and internal (copolymerized) varieties. Interesting changes in mechanical properties have been observed in materials of this type [197]. [Pg.232]

It has been known since the early work of Farkas and Sachsse (6) that the ortho-para conversion may be catalyzed by paramagnetic species. That the mechanism for this kind of conversion is nondissociative is shown by the absence of hydrogen-deuterium equilibration at a comparable rate under similar conditions. But proof that the nondissociative [Pg.25]

Extrinsic field effects have been studied on a large number of solid catalysts of quite diverse magnetic properties. Presentation of results on these substances will be started with four oxides that are normally considered to be diamagnetic. [Pg.26]

In the preparation of La203, and of all other rare earths, a problem may [Pg.26]

From Fig. 3 it is clear that the conversion rate is very sensitive to the applied field in the 4 Oe region. If the current through the solenoid is adjusted to produce a field of 4 Oe in the same sense as the Earth s field, then the resultant field at the reactor is about 4.6 Oe. If now the solenoid current is reversed the resultant field becomes 3.4 Oe. This change is easily measurable as shown in Fig. 4. The result shown was actually observed on a dilute lanthana-supported erbia catalyst sample but similar results may be obtained on activated Lu203 with more convenience. These results show that the Earth s field could be measured by making [Pg.28]

Fractional (%) rate decrease vs. applied field to 10 kOe (log scale) over Y2Oa heated in H2 at 823 K. Measurements at 298 K. [Pg.30]

The activation energies corresponding to the y and fi processes, Eay and Eap, are listed in Table 6, together with the activation entropies, A Say and ASap, calculated according to the Starkweather analysis described in Sect. 2.3. The low values of the activation entropy (10-20 J K-1 mol-1) obtained for the y transition means that this transition deals with localised motions. The ft transition, which has a higher activation entropy (50-80 J K-1 mol-1), should correspond to motions with some cooperative character. [Pg.115]

The activation energy and entropy of the /i transition in MT are listed in Table 6. The activation energy, a/i is very similar to the activation energies determined in xly -y polymers for the /i transition. In contrast, the activation entropy is quite low, indicating that the ft transition of MT is less cooperative than the fJ transition of xTy 11 polymers. [Pg.116]

COMPUTING ANISOTROPIC LOCAL SPACE AVERAGE COLOR [Pg.268]

Owing to the extent of the smoothing, the output computed using local space average color is not as good when compared with the output computed using anisotropic local space [Pg.271]

Eight trials using agarose gels were performed for each of the seven decompression schedules, and the total number of bubbles formed per gel sample (0.27 ml) was recorded. Table 8.1 lists the number of bubbles (mean S.E.M.) observed with each decompression profile at various depths, i.e., stops . [Pg.140]

The influence of the reactor temperature on the conversion of methane was examined during pulsed operation. The heat performance of the foil heater was slowly increased while the reactor was continuously supplied with gas pulses consisting of pure oxygen at 129.5 ml min-1 together with a flow of methane (0.5 ml min-1). The volume flow of the carrier gas nitrogen was adjusted to 130 ml min-1 at atmospheric pressure, delivering a residence time in the coated spiral of 0.4 s. The cat- [Pg.113]

This is consistent with the conversion values obtained earlier under steady operation with a platinum catalyst, ranging from 18 to 80%, depending on the pretreatment of the catalyst under similar residence times and temperatures. [Pg.114]

This activation energy is close to the 24 kj mol-1 reported by Mezaki and Inoue for the methane oxidation at a platinum catalyst on an alumina substrate at temperatures above 350°C. [Pg.115]

In the literature, higher values for the activation energy are also found [82, 83]. One reason for this could be the neglect of a pre-reduction of the platinum catalyst and also the low porosity of the sputtered catalyst. Another possibly important aspect is that here we actually measured intrinsic kinetic data compared with the diffusion-affected kinetic data in refs. [82] and [83]. [Pg.115]

On one hand, the observed differences (1.46 times at 1173 K and 1.3 times at 1123 K) may be viewed as standard for ceramic samples [5]. On the other hand, they [Pg.503]

The main result of the experimental part of the study, which is shown in Fig. 4, confirms the supposition, which was made in the Introduction above, that one cannot expect formation of structural vacancies in the oxygen sublattice of strontium-alloyed Lai-ySryMnC -s perovskites and, correspondingly, a considerable increase [Pg.504]

the result obtained for D(y) is due only to a decrease in the concentration of JT ions in the strontium-alloyed samples (some Mn3+ ions change their valence to Mn4+). It will be used below when we discuss the effect of JT deformations on the oxygen diffusion coefficients. [Pg.505]

If the difference between dimensions of the anion and the passage at the saddle point, anion — R 0i is comparable with local JT displacements mjx (10—1 —10 2)/ anion, the D value should increase considerably as compared toD° at temperatures kBT A(A lO-1 eV). [Pg.506]

One may expect that non-isovalent substitutions in these systems should cause a considerable decrease in the diffusion coefficients. This is due to a drop in the total number of degenerate centers and a simultaneous decrease in the concentration of degenerate centers having a relatively long relaxation time. Then for dilute systems with y 1 the following value of ratio between the diffusion coefficients D(y)/D(0) takes place D(y)/D(0) = 1 — yz, where z is some coordination number. As is seen from Fig. 4, for y = 0.075 that value agrees fairly well with an experimental result D(y = 0.075)/D(y = 0) = 0.46 at a reasonable values of z (for example, D(0.075)/D(0) = 0.4 at z = 8). [Pg.506]

In this section, only general findings will be discussed which are valid for all packings investigated. Differences between the monolith types or between distillation packings and monoliths, which can be explained by the different flow patterns, are discussed in Section 8.4. [Pg.253]

For the coating of the DX-packings, slight deactivation can be assumed, as the DX-packings had already been used and recalcined several times. [Pg.253]

The reported values of the diffusion coefficients of cations in zeolites are around 10 13-10-15 [m2/s] [5,37,48], and the factors which affect the velocity of cationic exchange are [Pg.353]

we report kinetic data measured during the ion-exchange process in the NH4 -Ni2+ system in the sample CMT-C [5,37], CMTC-C was obtained from deposits located in Tasajeras, Cuba (see Table 4.1) [5], The parameters characterizing the kinetics of ion exchange of NH4 and Ni2+ in the sample CMT-C [5,37], that is, R, De and the TEC, are reported in Table 7.3. [Pg.353]

Concerning the use of CVD ZnO films as buffer layers between the absorber part of the cell and the front TCO (see Sect. 6.3.1.1), highly resistive [Pg.290]

To improve the junction property between CIGS absorber/Zn(0,S,OH)j and ZnO B window, Sang et al. [55] inserted an undoped thin CVD ZnO layer between the Zn(0,S,0H)a buffer and the ZnO B window. They observed an increase of both the Voc and FF, leading to a 30 x 30 cm2 submodule (aperture area = 864 cm2) with 12.93% efficiency. Finally, Olsen et al. [67] reached an efficiency of 13.95% (aperture area 0.13 cm2) for CIGS solar cells using a CVD ZnO buffer layer (see also Chaps. 4 and 9). [Pg.292]

Wenas et al. [70] suggested that desorption of H2O from LP-CVD ZnO B deposited at low temperature during the subsequent growth of the amorphous silicon layer could damage the ZnO/p-layer interface. Indeed, as illustrated in Fig. 6.52, they observed an increase of all the a-Si H solar cell [Pg.292]

Finally, Wenas et al. [72] also proposed a two-step LP-CVD process in order to smoothen the too sharp surface morphology of as-grown LP-CVD ZnO by depositing a thin layer of flat LP-CVD ZnO layer grown with DEZ/ethanol/H20 reactant. By varying the thickness of both layers, various surface morphologies have been obtained, which can be suitable for thin film silicon solar cell deposition. [Pg.293]

Loffler et al. successfully deposited a-Si H solar cells on their in-house ZnO grown by expanding thermal plasma CVD [52]. They reached initial efficiencies of around 10%, and supported also the need to improve the ZnO/p-layer interface. [Pg.293]

A device with a 35-/im gap was also examined and a 20-kHz operation was observed. [Pg.171]

When analyzing the operation of a-Si H devices, the localized states must be taken into account. In this chapter the transfer inefficiency of a-Si H CCDs is evaluated numerically and analytically on the basis of the assumption that the localized states in a-Si are distributed exponentially in energy. We have clarified that ln(e) versus ln(/) is linear and that its coefficient is determined by Ta and T. This feature agreed with our experimental results. And the rate equation and the conservation equation used in this analysis can be applied to a-Si H FETs. [Pg.171]

The resistively connected gate a-Si H CCD described in this chapter operates at high clock frequencies. A 10-/an-pitch device operated at 200 [Pg.171]

I would like to thank Mssrs. S. Kishida and Y. Uchida for their collaboration and Profs. S. Furukawa and K. Takahashi of Tokyo Institute of Technology for their encouragement. A part of this work was supported by the Ministry of Education, Science, and Culture of Japan with a Grant-in-aid for Special Project and Scientific Research by Hoso-Bunka Foundation, and by the Research and Development Corporation of Japan. [Pg.172]

In this chapter we describe modifications of chemically stable materials to achieve sensitive archival storage media. The following sensitizing approaches will be discussed incorporation of a gas component into the atomic network in bound form, texturing of the media surface, and electrically amplified writing. [Pg.173]

From the observed increase in the oxidation current, and decrease in the reduction current, it is clear that these modified films are catalytic surfaces for NADH oxidation at pH 7. With time, the current decay seen at pH 5 is no longer evident at neutral pH, as predicted if the degradation is mainly due to acid catalysed NADH decomposition. In Fig. 2.16, the [Pg.62]

Analytical models of modified electrodes for NADH oxidation [Pg.64]

The time required for the electrode to attain a steady-state response after addition of an aliquot of NADH is of the order of seconds (—10 s for a film held at 0.1 V). Comparing this response time with those obtained in the mass transport-limited regime for a standard couple at a bare electrode, it is clear that the response time of the modified poly(aniline) electrodes is of the order of the mixing time for the system. [Pg.64]

The excellent stability and reproducibility of these modified poly(aniline) electrodes for NADH oxidation allows detailed kinetic studies of the system to be completed. To determine the mechanism of NADH oxidation the effects of film thickness, electrode potential, rotation rate and NAD concentration have been investigated. [Pg.65]

the effect of film thickness on the amperometric response was studied. The effect of film thickness has been assessed for eight different film thicknesses at four different NADH concentrations. For thin films, Fig. 2.18 shows that the response increases with film thickness reaching a [Pg.65]

Several chemical and physical treatments have been used to identify the oxidation photoproducts that generate these IR absorptions [7,8]. The purpose of chemical derivatization reactions (with reactive gases such as NH3 or SF4 or methanol) or of a physical treatment (photolysis or thermolysis in the absence of oxygen) carried out on pre-photooxidized samples is to modify the IR spectrum of the oxidized samples by producing a decrease in some specific absorption bands and eventually creating new ones. This technique is very useful for locating the maxima of convoluted IR bands. Several examples of such treatments are given in this chapter. [Pg.705]

In the hydroxyl domain, the absorption is almost completely lost. These data were compared with those obtained for model compounds introduced by permeation in PS films and then submitted to SF4 for 1 h. The results reported in Table 30.1 show the position of the maxima of the carboxylic acids and their [Pg.705]

The photoproducts formed in the PS films during irradiation at A 300 nm were identified using various chemical and physical treatments. In addition to the reactions with SF4 and NH3 treatments with methanol, thermolysis and photolysis experiments were carried out on photooxidized samples [7]. In the light of all those tests, it was concluded that numerous photoproducts formed are low molecular weight species. Those products were volatile and may diffuse out of the film. [Pg.707]

The abstraction of a hydrogen atom occurs preferentially at the tertiary carbon of the structure, leading to a polystyryl radical. This radical adds to oxygen to form a peroxy radical. By abstraction of another hydrogen atom, the peroxy radical leads to a hydroperoxide. Hydroperoxides have an IR absorption at 3450 cm-1. The decomposition of the hydroperoxide either by photolysis or by thermolysis gives an alkoxy radical that may react in several ways  [Pg.707]

The end-chain aromatic ketone (1690 cm-1) may react photochemically by a Norrish type 1 reaction, leading to the formation of benzaldehyde (1704 cm-1) and benzoic acid (1698-1732cm-1). No detailed mechanism can be proposed for the formation of benzoic anhydride (1725-1785 cm-1) since several plausible routes exist. [Pg.709]

As a general statement, isomerizations occur much slower (around lOOtimes and more) in the film than in solution. It was already observed for azo compounds by Kamogawa et in the case of copolymers of 4-vinyl-4 -dimethylaminoazobenzene (I) with styrene and of 4-acryloylaminomethylaminoazobenzene (II) with styrene, butyl acrylate and methyl methacrylate. [Pg.19]

The dependence of the rate of decoloration on temperature, espedally around the ass temperature, will be considered in Sect. [Pg.19]

It has been observed for spirobenzopyrans as well as for azo compounds that, when dissolved in bulk polymers or linked to the latter as side groups, the plot of the logarithm of the optical density versus time shows strong deviations from first-order kinetics. Thus, the decoloration of a film of a copolymer of l-(/8-methacryloylosyethyl)-6 -nitro-DIPS with methyl methacrylate after irradiation is represented in Kg. [Pg.19]

Such rate of decoloration was initially interpreted as being the sum of two or three exponential rate proc ses, each char terized by its own rate constant (kj k2 ks), which should correspond to a different merocyanine isomer (Kg. 2). [Pg.19]

1 DIPS designates 3,3-dunethyl-spiro-2H-l-benzopyran-2,2 -indoline [Pg.19]

The thickness of the epitaxial layer depends on the temperature, solvent, cooling rate and amount of solvent and silicon, i.e. the weight of the melt compared to the surface of the substrate. [Pg.141]

The experiments were done under the following conditions 7 g of Sn (purity 5N), 2h of growth, 0.5°C min-1 cooling rate. Since the amount of silicon incorporated in the melt increases with the temperature, it is possible to grow thick epitaxial layers. However, for low-temperatures (700-800°C), incorporation of silicon is low and limits the kinetics of growth. At this temperature range, thermodynamic properties of metallic alloys can increase the kinetics (see Sect. 9.6). [Pg.142]

If we use moderate cooling rates (0.25°C min-1, 0.5°C min-1 and 1°C min-1), experimental results presented in Fig. 9.3b show that the final thickness is independent from the cooling rate and depends only on the temperature drop (undercooling). [Pg.142]

Moreover, the cooling rate also influences the quality of the epitaxial layer Solvent inclusions and surface ripples appear when cooling rate is above [Pg.142]

1°C min-1. Therefore, to obtain flat surface and thick epitaxial layer in a reasonable time, growth rates of 0.5-l°C min-1 are commonly used. We did not observe that addition of Ga in the melt modifies the growth rate noticeably. [Pg.143]

The mathematical model of FCC feed optimization described in section 9.2.3 was programmed in MATLAB model-files where the various constraints were formulated as objective components in the hard form. Applying the duality principle, the various maximization objectives were converted to minimization functions by simply negating them (Dantzig and Thapa, 1997 Deb, 2001). These model files were linked to the MOEA Toolbox to obtain the optimized values for the various control variables. LP was also applied and its solutions were used as a basis for comparison. [Pg.288]

To provide the decision maker insights into the characteristics of the problem before a final solution is chosen, eleven different solutions from Pareto optimal set were considered Tables 9.2 and 9.3 list their objective and constraints values and their corresponding flows of the individual feeds respectively. For comparison, Tables 9.4 and 9.5 give the results obtained from linear programming in the Honeywell DCS system. [Pg.290]

Due to the complicated situation in mixed HC1/HF solutions with the possibility of forming mixed chloride/fluoride or fluoride complexes, it was advisable to repeat the experiments in the pure HQ system (Pershina et al. 1994). [Pg.232]

In the frame of the REHE project, the amine extractions of the group 5 elements were systematically revisited by Paulus etal. (1999). Pershina (1998b), by considering the competition between hydrolysis and halide complex formation, predicted the extraction sequence [Pg.232]

In the system Aliquat 336/HF, the reaction products were loaded onto the column in 0.5 M HF. In elutions with 4 M HF (Pa fraction) and with 6 M HNO3/O.OI5 M HF (combined Nb, Ta fraction) all a-decay events of element 105 were observed in the Nb, Ta fraction. This results in a lower limit for the K value of element 105 in 4 M [Pg.232]

HF of more than 570, which is close to that of Nb and Ta ( 103) and differs markedly from that of Pa ( 10). [Pg.233]

To conclude, the amine extraction behaviour of dubnium halide complexes is always close to that of its lighter homologue Nb, in agreement with the predicted inversion of the trend of the properties when goingfrom the 5d to the 6d elements (Pershina 1998b Pershina et al. 1994). In pure HF solutions, it differs mostly from the behaviour of Pa. In pure HC1 solutions, it differs considerably from both Pa and Ta. In mixed HC1/HF solutions, it differs markedly from the behaviour of Ta. The studies of the halide complexing and amine extraction of the group 5 elements both theoretically (Pershina [Pg.233]

In the following we discuss measured hysteresis effects occurring in OFETs and in the corresponding MIS capacitors. For this purpose measurements are presented which are representative of the different devices prepared by us. [Pg.320]

As we mentioned earlier, the choice of / in the cost function actually suggests a continuously distributed tradeoff between two design objectives, wire length [Pg.107]

AM 149 Distribution of Wirelength and Maximum Temperature Difference PurcArea/WircIcnglh Driven [Pg.109]

Cosl/Iblal Initial Cost=7% Temp. Ccisi/Total Initial t ost -16% [Pg.109]

Design Measures of merit Area wire length driven Area, wire length thermal driven [Pg.110]

Our floorplanning tools could serve as the prototype for future 2.5-D system designs. A full-fledged 2.5-D floorplanning tool should be equipped with many new feature features described as follows. [Pg.112]

The physicist who studies polymers in solution must determine how the osmotic pressure varies with concentration. [Pg.158]

We can thus take a mass Jt, of solute and a given volume of solvent (the total volume). Let us put these quantities in the osmometer schematically represented on Fig. 5.4. From hl we deduce the volume V of cell I. We shall assume that the solution is incompressible. The mass concentration of the solute is [Pg.158]

let us interpret these results by using Van t Hoff s law which is valid for very dilute solutions. The synthetically produced sample is polydisperse. We represent by the number of molecules of molecular mass which it contains. [Pg.158]

The quantity Mn is called the mean molecular mass. If the sample is made of identical particules with the same molecular mass M, then Afn = M. [Pg.159]

The value M corresponding to a given sample, is obtained from measurements of the osmotic pressure and of the mass concentration. In fact, we have [Pg.159]

During the SRC-II tests, the flow velocity in a vertical recycle line was varied by changing the pump speed from 300 to 800 rpm. The spectra of the Doppler signals are shown in Fig. 5-12 and the processed data are shown in Fig. 5-13. The voltage output of the flowmeter, which is related to the comer frequency of [Pg.177]

Based on the above results, we conclude that an ultrasonic Doppler flowmeter applicable to flows that contain suspended solids can be designed for both turbulent and laminar flows, but requires further development if excess gas bubbles are present. [Pg.178]

In all three experiments, Cr(VI) underwent a substantive decrease in concentration, and the distribution of Cr(T) was modified, indicating the widespread mobilization of chromium and the extensive coeval reduction of Cr(VI) to Cr(III). Accumulation of chromium in the anode chamber shows that electromigration was the predominant driving force for the transport of ions (e.g. Mukhopadhyay, Sundquist, and Schmitz, 2007). Generally, under neutral or high pH conditions, Cr(VI) exists as the soluble and mobile CrOi ion (Reddy et al., 2003) and,to a lesser extent, the dichromate ion Cr207. Reaction of the dichromate ion and the chromate ion to chromic acid occurs only under strongly acidic conditions (e.g. Mukhopadhyay, Sundquist, and Schmitz, 2007) and were most likely not attained in this study. [Pg.187]

Electrokinetically driven iron mineralization originates when Fe(III) combines with OH ions produced at the cathode to form insoluble ferric hydroxides [Fe(OH)3(s)], hematite ( -Fe203) andgoethite (FeOOH) (e.g., Faulkner, Hopkinson, and Cundy, 2005 Mukhopadhyay, Sundquist, and Schmitz, 2007). SEM observations of soil samples taken from the anodic zones of the experimental cells reveals a ubiquitous association between the iron minerals and subsidiary quantities of chromium. Cr(III) can substitute for Fe(III) in the FeOOH structure (Eary and Rai, 1988), and Cr(VI) reduction by Fe leads to the development of solids at nearneutral pH showing mixed iron/chromium solid solution of the form Fe Cri x(OH)3 (Eary and Rai, 1988 Fendorf and Li, 1996). Such conditions would have been met at the interface between the acidic and alkali portions of the experimental cells (Fig. 8.5). When Fe(III) is produced solely from the stochiometric reaction with chromate, the value of x is 0.75 (Batchelor et al, 1998)  [Pg.189]

However, in natural environments, soil-specific characteristics means that fractions of Fe(j,q), liberated by anode dissolution, will be rendered unavailable to react [Pg.189]

The highest residual traces of Cr(VI) occur in the anodic sections of the experimental cells. Cr(VI) removal from aqueous solutions is enhanced by the presence of ferric iron oxyhydroxide phases, as Cr(VI) adsorbs onto FeOOH (e.g. Aoki and Munemori, 1982 Mesuere and Fish, 1992a,b Mukhopadhyay, Sundquist, and Schmitz, 2007). The amount of released by anodic electrode dissolution primarily depends on the applied current and the duration of the passage of the current through the electrodes (e.g. Mukhopadhyay, Sundquist, and Schmitz, 2007). Differences in the lateral extent of iron mineralization in the three experiments illustrate that the buffering capacity of the soils influenced the spatial extents of the zone of Cr(VI) reduction and complementary alkaline zone. The Warwick soil (experiment A) operated at half the applied voltage to experiments B and C, experienced the furthest advance of iron mineralization from the anode array, quickly developed a sharp pH jump, and attained the most acidic conditions. Collectively, these attributes indicate that the Warwick soil had a comparatively low buffering capacity relative to the other two soils examined. [Pg.190]

The high buffering capacity of the Lanarkshire soil (experiment B) compared with experiment A, is demonstrated by the limitation of acidification and associated iron staining to within -lOcm of the anode. However, a pH jump did emerge after 3 weeks, with alkaline conditions prevailing in -60% of the experimental cell. The 96.8% reduction in the Cr(VI) content of the cathode zone, as well as the 84.4% decrease in the anodic zone, suggests that stabilization was advanced. The complementary 25.8% increase in Cr(T) around the anodic array, as well as the associated 17.4% reduction in Cr(T) around the cathode array (Fig. 8.3), is consistent with the anodic domain operating as an efficient localized zone of Cr(VI) reduction to Cr(III). [Pg.190]

1 Stable Node In CPMs, many different entering liquid compositions [Pg.96]

FIGURE 4.5 A residue curve map for the diethyl ether/benzene/methanol system generated using the NRTL thermodynamic model at P s 0.825 atm. [Pg.97]

FIGURE 4.6 Experimental validation of rectifying column profiles for the benzene/diethyl ether/methanol system with the reflux ratio r== 3 and x/ = X d = [0.694, 0.066] using the NRTL thermodynamic model at P=0.825 atm. [Pg.98]

Firstly, we have tried to assess the effects of a variation in oxygen partial pressure on the two zones of the sensor, that is, the internal zone (marked 1) and the external zone (marked E). [Pg.291]

In practice, we have chosen to study two kinds of atmosphere an atmosphere with 1% oxygen and an atmosphere with 20% oxygen. In both cases the oxygen is diluted in nitrogen. [Pg.291]

These effects are entirely reversible, as indicated by the results reported in Held C. [Pg.291]

These results were expected, given the nature of this oxide the conductivity decreases when the quantity of chemisorbed oxygen increases. [Pg.291]

This is because the concentration of the ionized vacancies and, subsequendy, of the free electrons stemming from the ionization of these vacancies decrease with the oxygen pressure. [Pg.292]

General.—Activity coefficients at infinite dilution of many systems have been measured by g.l.c. and compared with static measurements. The agreement has been excellent for those systems where no surface adsorption has been present. Activity coefficients obtained from g.l.c. must therefore be held suspect unless care has been taken to show the absence of surface effects. [Pg.60]

The results prior to 1967 have been well discussed in reviews by Young and Kobayashi et al Many of these results were obtained from ill-defined substances such as silicone oils and apiezon greases and will not be discussed here. [Pg.60]

Task/ Task description Standard time STj is) Theoretical no. of operator assignment Actual no. of operators assigned Theoretical operative assignment k [Pg.163]

This line balancing optimization problem has the following assumptions  [Pg.164]

In this study, the aim is to investigate whether genetic optimized operative assignment can reduce the apparel assembly makespan when compared with theoretical operator assignment. It is also intended to compare the performance of different levels of skill inventory, 57, on the makespan in order to determine the optimal number of task skills an operator should have in the assembly process. The proposed method is applied to adjust the operative assignment hourly so that [Pg.164]

7 Genetic optimization performance of a particular run (seed 4) when optimization was based on system status at t= 50400s. [Pg.165]

Two error metrics are defined to provide quantitative comparison between the different control schemes. Given a starting time to and a constant T 0, the normalized average error Ca is defined as [Pg.135]

We choose T to be 100 s. Under the robust adaptive control scheme, Co dropped from 11% at to = 0 h to 7% at t = 4 h, and e dropped from 15% to 9% for the same period. In comparison, Ca increased from 7% to 28% under the PID controller, from 7% to 50% under the fixed model-following controller, and Cm increased from 8% to 25% under the PID scheme, and from 10% to 48% under the model-following scheme. Fig. 5.11 further shows the evolution of Ca and Cm, calculated every half a hour, under the three schemes. It is clear that the robust adaptive control scheme delivered consistent tracking performance during the four-hour continuous operation, while the tracking performance under the PID scheme or the fixed model-following scheme deteriorated over time. [Pg.135]

During the capture step, the temperature at the outlet of the bed is almost stable at the initial bed temperature (approximately -130 C), but increases strongly as soon as CO2 starts to breakthrough. When the bed is at a temperature of -100 °C, the capture step is stopped. When the recovery step is started, it can be observed that the temperature increases quickly to a temperature of approximately -76 C corresponding to a saturation temperature of pure CO2 at the operating pressure (1.2 bar). [Pg.35]

2 bar is measured, which is slightly changing during the step and is likely related to the changing gas phase temperature in the bed. [Pg.36]

During all steps, the pressures at the inlet and outlet of the beds have been monitored. It is observed that the pressures at the inlet and outlet are virtually equal during all the three steps, meaning that the pressure drop over the packed bed is negligible compared to the pressure drop over piping/valves, etc. [Pg.36]

If cyclic molecules are present during the end linking of chains, some will be trapped because of threading by the linear chains prior to the latter being chemically bonded into the network structure (figure 7.28). - The [Pg.177]

Ligand Field Splitting Parameters for Motybdennm Hexacarbonyl [Pg.28]

Ligand Field Stabilization for Complexes of Molybdennm Hexacarbonyl and Poly(vinylamine) in the Glassy State [Pg.29]

Quantum Mechanical Model Parameters and Trigonal Bipyramid 5-Coordinate d Complexes of Molybdenum Hexacarbonyl and Poly(vinylamine) with D3h Symmetry Above Tg [Pg.29]

In these expressions, (r ) represents the average (i.e., expectation value) of r with respect to the radial part of the d-electron wavefunctions, r is the radius of the electron cloud about the metal center, and L is the metal-ligand bond distance. There are five 3d-orbital wavefunctions, and each one exhibits a different spherical harmonic expression in terms of polar angle 0 and azimuthal angle (p in spherical coordinates. [Pg.29]

However, the radial part of each 3d-orbital wavefunction p (r) is the same, as given by  [Pg.30]

The first to report the concentration dependence of halide ion quadrupole relaxation in aqueous solutions of strong electrolytes were Itoh and Yamagata [247]. Their and later studies have shown that whereas the change in relaxation with concentration may depend greatly on the cation present, the relaxation rate at low concentrations is independent of cation. For aqueous solutions of alkali halides, the concentration dependence of the anion quadrupole relaxation rate is in most cases weak below ca. 1 M. Consequently the relaxation rate in the [Pg.106]

Br relaxation rate at infinite dilution by measuring T.j using the 180-T-90 pulse sequence. They obtained at 25°C, VT q = 1050 s .  [Pg.107]

Determinations of T from the line width have invariably led to [Pg.107]

1500 s [52 238 239]. Other line width studies have given relaxation [Pg.107]

Hertz and Dr. Weingartner have recently informed us about improved line width studies in agreement with our data. [Pg.107]

A large amount of research has been reported on the mechanical properties of CNT reinforced plastic materials. In the early days, pristine CNTs were mostly used to fabricate CNT nanocomposites. The PMMA nanocomposites were prepared by melt blending, and the nanotubes were well dispersed in the matrix with no apparent damage or breakage. The storage modulus of the PMMA matrix is significantly increased by the incorporation of pristine MWNTs, particularly at high temperatures [90]. [Pg.231]

Polymer/CNT composite nanofibers can be fabricated by melt processing (such as extrusion, spinning and electrospinning) and solution processing (such as spinning and electrospinning) approaches. [Pg.235]

Gao et al. reported a chemical processing technology that allows the continuous spinning of PA6/SWNT fibers by the in situ polymerization of caprolactam in the presence of [Pg.235]

Despite significant reinforcement of PC, the level of reinforcement is far below what conld be achieved if the nanotubes were completely dispersed and aligned along the fiber axis as predicted by composite theory. [Pg.237]

The structural changes during deformation of solution- and gel-spun PAN/CNT nanocomposite fibers were also investigated by using synchrotron X-ray diffraction [129]. The deformation of CNTs is shown to contribute to the increased modulus. CNTs, in addition [Pg.237]

In Fig. 4.6b, the control parameter vector 0 k) has stabilized after about 8 s and before the deadband is reached. [Pg.60]

The final values of the controller parameters are given in Table 4.1. [Pg.60]

Experiments were performed with long cylindrical or conical pieces of responsive gels hanging in a tubular CSTRs in which a strong recirculation of the fluid contents provided a uniform chemical composition around the gel [13]. These geometries minimize the mechanical constraints imposed by the anchoring of the gel inside the CSTR. However, the additional nonradial dimension unavoidably introduces additional dynamic complexity, and the spatiotemporal behavior of the system becomes richer, as we shall see. [Pg.182]

The sources of chemomechanical instabilities described above have been tested in two quite different proton-autoactivated systems the CT [63] and the BS [64] reactions. [Pg.182]

During this reaction large amounts of protons are released in accordance with the following balance equation  [Pg.182]

In the range of reactant concentrations experimentally explored, the reaction is very sluggish if the initial pH of the solution is above 7, whereas when pH 6, it very rapidly drops to pH 2. When operated in a CSTR, the reaction exhibits steady-state bistability, with pH differences between branches up to ApH 8), and does not lead to kinetic oscillations. However, in an OSFR, it was shown to display a diffusion-driven oscillatory instability because of the long-range activation of the free protons. But this instabihty can be quenched by weakly buffering the system with a low-mobility proton-binding species [58]. This condition is straightforwardly [Pg.182]

AuyoZnso (annealed at 500 C for 6 h). (b) Detailed spread of markers for the same system. [Pg.167]

By using the relationship that links the Young s elastic modulus (E) to the bulk (k) and to the shear (p) elastic moduli that reads  [Pg.95]

By posing that the PVME actuator exerts zero force at 36 °C, the stress generated by its temperature change is reported in Eigure 4.7. [Pg.95]

FIGURE 5. Shear and extensional viscosity of lUPAC A low-density polyethylene. (From data of Laun and Munstedt.( )) [Pg.85]

The signal source pulse I (t) was simply a rectangular pulse of 1-msec duration. Pulse amplitude could be varied from 0 to 10 V peak without overloading the amplifier system or affecting the linear range of the electrode polarization impedance. In each of the photographic records which follow. [Pg.75]

In the situations described in the present chapter, there are several lengths that may characterize the static or dynamical properties of a meniscus  [Pg.319]

It is of great importance to determine the relevant characteristic lengths depending on the experimental situations. This is an open question. In the following, we bring some indications on this issue. [Pg.319]

Many properties of water have been covered in a number of general sources of information,and we will make numerous references to specific chapters in these books. In addition, the International Association for the Properties of Water and Steam (Palo Alto, CA) has prepared critically evaluated representations of water properties that are intended to provide a basis for technical and scientific calculations.  [Pg.189]

The basic compilation of thermodynamic properties of water, covering a wide range of states, is found in the Steam Tables. We have summarized some commonly used values that are relevant for gas phase properties in Table 1 and likewise for liquid water properties in Table 2. It is noteworthy that the OH [Pg.189]

The dielectric properties of water are known over an extensive range of densities and temperatures. As noted above, the dielectric constant is sometimes used to assess a model s predictive ability. The dielectric constant is a smoothly decreasing function of increasing temperature and decreasing density. [Pg.190]

Nuclear magnetic resonance (NMR) spectroscopy is an especially useful molecular probe of water properties. The self-diffusion coefficient of water Dg has been measured, using a spin-echo technique, over a considerable range of temperatures and densities. This method complements the more direct tracer diffusion method. With one interesting exception, Dg increases with increasing temperature and decreases with increasing pressure. The exception occurs for temperatures in the 275-323 K range and for pressures up to about [Pg.190]

The dipole moment of a water molecule is 6.17 x 10 ° C m (1.85 D). ° By itself, this information is seldom used to develop parameters for water models, because the effective dipole moment of a molecule in a liquid environment is significantly larger. The exception to this statement occurs when the explicit many-body interactions associated with induced polarization are included in the model. [Pg.191]

Two sets of data are used to assess the accuracy of the monitoring system. Both sets of data were collected with four laser scanners placed in the lobby of a high school. Students move and interact in different ways in the lobby. The first data set includes students and their parents with a waiting line which lasts for approximately 30 min. In the second set of data, 300 people were invited to walk and run, following a prearranged script describing various social behaviors to perform for a duration of two hours. Data sets each provided their own set of challenges. However, the most difiicult to resolve are  [Pg.140]

Case 1 People walk closely. This is a case that happens very often, especially in a crowded environment. Because lasers distributed the points, the clustering based on a single image frame cannot correctly extract the target. [Pg.140]

Case 2 Two people from opposite directions and their feet are too close to the intersection points. The data are mixed and a person can be lost in the extraction. [Pg.140]

Case 3 Temporal occlusion with loss of data. [Pg.140]

Typical curves showing the total liquid hold-up hL can be seen in Fig. 2-2b for 25 mm metal Bialecki rings and Fig. 4-4a-d for selected types of packings with different gas capacity factors Fy, and the specific liquid load ul as the parameter. The influence of the liquid load ul on the liquid hold-up of randomly filled Pall rings is shown in Fig. 4-5a-c, the influence of the packing size in Fig. 4-5a,b and the influence of the material in Fig. 4-5c. [Pg.191]

the modified correlation (4-20) by Berner and Kalis [12] was used to calculate the hL value for ReL 2, using a correction factor of 3/4, see Chap. 2. This numerical value was the result of an evaluation of the available experimental data in the database. [Pg.193]

Equation (4-32) was used to determine the liquid hold hL for turbulent liquid flow Rcl 2. This equation is obtained by substituting the Froude number of the liquid, according to Eq. (4-31), into Eq. (4-26). [Pg.194]

The numerical value of Cp = 0.57 was found by evaluating experimental data, contained in the database, for randomly filled packing elements and structured packings of type Y, in the flow range of Rep 2 to Rep 200. [Pg.194]

In the case of structured packings and stacked packing elements of type X, the following constant Cp was found, independent of type and material  [Pg.194]

In Fig. 2.7, the measured Lb,c1 distribution for z 5 cm is also approximated satisfactorily by the empirical correlation of Xie et al. [23] The measured LB,d value obtained at z = 1 cm is much larger than 2 cm, implying that the bubble generation region extends far beyond z = 2 cm. Consequently, the measured B,d value in the close vicinity of the nozzle exit does not present the real bubble [Pg.24]

The radial distributions of gas holdup, a, measured by Iguchi et al. [24] at four representative axial positions are shown in Fig. 2.8. The a distribution at z = 1.5 cm is very steep near the centerline of the bubbling jet. Two peaks appeared in the a distributions measured at z = 4.0 and 7.0cm. These two peaks are not caused by the swirl motion of a bubbling jet because no swirl motion was observed under the [Pg.25]

Although any evidence is not given, agreement between the measured a values and the empirical correlations is not good at z = 4.0 and 7.0 cm because these two correlations assume Gaussian distributions. The measured radial distribution of a approached a Gaussian distribution as z increased further (see a distribution at z — 10 cm). As a result, the measured a values at z = 10 cm were approximated adequately by the empirical correlation by Iguchi et al. [6,7], as demonstrated in Fig. 2.9. [Pg.26]

In Fig. 2.10, showing the radial distributions of bubble frequency /b, a plateau appeared in the distributions at z = 4.0 and 7.0cm. This is also attributed to the formation of bell-shaped bubbles [25]. The radial /b distribution measured at [Pg.26]

A reexamination of previous experimental results for an Fe-Ar system, [2,3,5] a Cu-Ar system [4], and a Wood s metal-N2 system [26] reveals that the radial distributions of a, /b, Mb, and Lb are similar to those mentioned above near the nozzle exit, although each radial distribution is not so distinguished compared with the results presented in Figs. 2.12 and 2.13. [Pg.27]

The first major observation of ionic current across the interface between two immiscible solutions was reported by Nernst and Riesenfeld, who in 1902, studied the transport of colored electrolytes across water-phenol-water concentration cells. However, it was only in 1974 that Gavach et al applied what we could call [Pg.11]

Having realized how much information could be gained by applying electrochemical techniques to the study of ion transfer reactions, Gavach et al went on investigating the transfer of a series of tetraalkylammonium ions (TAA ) for the following systems  [Pg.12]

Working with higher current densities, ranging from 10/iAcm to 100 they studied the kinetics of the transfer reactions. [Pg.12]

Assuming that the concentration of the transferring ion in the organic phase was constant, and assuming that the current versus voltage relationship obeys a Butler-Volmer law  [Pg.12]

The experimental results obtained appeared to validate the Butler-Volmer assumption, and the standard rate constants, k°, can be recalculated from the published data of k, and kl, and a as being equal to 0.0022, 0.0023, and 0.0048 cm s for tetraethyl-, tetrapropyl-, and tetrabutylammonium, respectively, knowing that [Pg.13]

The FH parameters Th and Fa for the PB copolymer blends are depicted in Fig. 10 versus the vinyl content of the protonated PB component. The solid and open triangles and spheres represent blends with fixed vinyl content of X = 0.07, 0.16, and 0.91 of the deuterated PB component, respectively. The FH parameters were corrected for chain-end effects which are rather strong and are not shown here (see Fig. 6 in [64]). [Pg.29]

The blend with x = 0.91 (dPB(l,2)) andy = 0.54 vinyl contents yields a relatively large enthalpic Th as already evident from the data in Fig. 9 on the [Pg.29]

The enthalpic part of the FH parameters appears very much influenced by the isotope effect, e.g., whether the PB(l,2) or PB(l,4) is deuterated or not. If one considers a PB copolymer mixture of only protonated components, using the van der Waals interaction parameters in Table 3 and setting [Pg.30]

The physical basis of the behavior of Fj, in Fig. 10 becomes more transparent if a simplified version of Eq. 22, namely Eq. 24, is used, which is [Pg.31]

The expression for entropic Fa in Eq. 23 describes the data with the X = 0.07 samples and the results by Jinnai et al. [75] very well assuming z = 5.7 nearest neighbors. Because of obvious Umitations inherent in any lattice model, the parameter z is allowed to vary freely to compensate for deficiencies of the model. The closeness of z = 5.7 to the theoretical z = 6 is, however, quite convincing. According to the theory, there seems to be no isotope effect on Fa. Deviations from theory were found for the dPB(l,2)/ PB(1,2 1,4) blend, which shows a positive F that cannot be described without possibly including chain semi flexibility effects. [Pg.32]

Aluminide coatings with lower aluminium contents were then developed. The coating temperature was kept at 715°C (for 6 h) and some changes in the pack composition were carried out in order to reduce the A1 activity in the gas phase. [Pg.180]

By using the more stable activator AICI3 instead of NH4CI at 715°C, the coating phase was shifted into the range of FeAl with up to 53 at.% A1 (Fig. [Pg.180]

The first layer of the coating is quite porous, the second layer is much denser with a composition varying from 45 at.% A1 to 26 at.% on the first 5 pm. The aluminium enrichment in the ferritic matrix reaches a depth of around 30 pm underneath the surface and leads to the formation of aluminium nitrides appearing as black needles. [Pg.180]

The same coating phase can be obtained at 650°C by replacing the pure A1 masteralloy by a powder of CrsAl intermetallic compound. The coating phase is less than 5 pm thick and shows some thickness irregularities. Its A1 concentration is in the same range as in the previous case with 53 at.% (Fig. [Pg.180]

The single element Si coatings are shown in Figs 10.6 and 10.7 for FBCVD and pack cementation, respectively. With the thickness of the enriched layer [Pg.180]

The anisotropic shear viscosity coefficients V2 3 t]i2 have been determined only for a few liquid crystals. In contrast there have been many investigations of the shear viscosity coefficient under flow alignment. The reason for this might be that the effort required to determine. the anisotropic coefficients is greater by far. Viscosity coefficients determined under flow alignment are often used to estimate the switching times of liquid crystal displays. For basic research they are less important. [Pg.150]

The behaviour of the coefficients rji, 1)2 d 773 will be discussed for a liquid crystal having a broad nematic range and no anomalies. A mixture of nematic liquid crystals with similar structures is well suited to this purpose, and the example used here is Nematic Phase V, a former product of Merck, which consists of a eutectic mixture of the two isomers of 4-methoxy-4 -/i-butyl-azoxybenzene (65 mol%) and the two isomers of 4-methoxy-4 -ethylazobenzene (35 mol%). The nematic phase ranges from 268 K (melting point) to 347 K (clearing point). The mixture exhibits a sharp clearing point. [Pg.150]

Tp amounts to 180 K for this liquid crystal. With the exception of the neighbourhood of the clearing point, the order [Pg.151]

The predicted relation between shear viscosity and degree of order is of the form [43] [Pg.151]

Direct comparison of experimental data and theoretical predictions is difficult. Like the case of isotropic liquids, there is no theory that allows the calculation of the reference viscosity fj for liquid crystals. Furthermore, experimental values for 54 are not known with sufficient precision. It has been shown empirically [44] that a relation of the form [Pg.152]


From the analytical results, it is possible to generate a model of the mixture consisting of an number of constituents that are either pure components or petroleum fractions, according to the schematic in Figure 4.1. The real or simulated results of the atmospheric TBP are an obligatory path between the experimental results and the generation of bases for calculation of thermodynamic and thermophysical properties for different cuts. [Pg.99]

The constants k- enable the improved representation of binary equilibria and should be carefully determined starting from experimental results. The API Technical Data Book has published the values of constants k j for a number of binary systems. The use of these binary interaction coefficients is necessary for obtaining accurate calculation results for mixtures containing light components such as ... [Pg.156]

Sufficiently accurate thermodynamic models used for calculating these equilibria are not available In simulation programs. It Is generally not recommended to use the models proposed. Only a specific study based on accurate experimental results and using a model adapted to the case will succeed. [Pg.171]

Experimental results on real ultrasonic B-scan data, acquired from samples with coarse material structure, are presented to demonstrate the power of the novel approach. [Pg.89]

The paper discusses the application of dynamic indentation method and apparatus for the evaluation of viscoelastic properties of polymeric materials. The three-element model of viscoelastic material has been used to calculate the rigidity and the viscosity. Using a measurements of the indentation as a function of a current velocity change on impact with the material under test, the contact force and the displacement diagrams as a function of time are plotted. Experimental results of the testing of polyvinyl chloride cable coating by dynamic indentation method and data of the static tensile test are presented. [Pg.239]

During the control, the reception coil has been scanning inside of the emission coils. The theoretical and experimental results have been obtained under the condition of a constant lift-off of 50 pm, obtained by applying a protective polyethilenic foil. [Pg.377]

Figures Absolute e.m.f. dependence of the probe vs. position for different sub-surface crack depths - theoretical and experimental results... Figures Absolute e.m.f. dependence of the probe vs. position for different sub-surface crack depths - theoretical and experimental results...
Finally, a FEM Analysis has also been perfonned and a very good agreement found with the experimental results. [Pg.408]

The first phenomenon is sedimentation of developer s particles in a zone impregnated with a penetrant. As a result the thickness of developer s layer h, appearing in formulas, is smaller than the thickness of dry zone. Our experimental results show that in some cases h is 80% smaller than h. The pictures illustrating the sedimentation influence upon the values of thickness for various developers are obtained. The estimation of this influence upon calculated sensitivity is carried out. [Pg.613]

Another phenomenon is so called two-side filling of one-side closed conical capillaries with liquid [5]. On the one hand the more penetrant is trapped by the defect the wider indication will appear. Contrariwise it is almost impossible to extract a penetrant from the completely filled surface defects by dry developer [6]. In this study we propose the theory of the phenomenon. Besides experimental results of the investigation of two-side filling with various penetrants of conical capillaries are presented. Practical recommendations to optimize liquid penetrant testing process are proposed. [Pg.613]

One more experimental result, which is important for PT is as follows. Only polar liquids fill conical capillaries from both sides. We used various penetrants to fill conical defects Pion , LZh-6A , LZhT , LUM-9 etc. It was established that only the penetrants containing polar liquid as the basic liquid component (various alcohols, water and others) manifest two-side filling phenomenon. This result gives one more confirmation of the physical mechanism of the phenomenon, based on liquid film flow, because the disjoining pressure strongly depends just on the polarity of a liquid. [Pg.618]

Tables I and 2 show the experimental results obtained for axial and transversal displacements respectively, where % is the displacement and Xv. is the displacement measured using our experimental. setup. Tables I and 2 show the experimental results obtained for axial and transversal displacements respectively, where % is the displacement and Xv. is the displacement measured using our experimental. setup.
Table 1 Experimental results obtained for D=(350 2) mm y Act=(5° 2 ). x is the axial translation and Xe is the experimental value obtained from Eq. (1). Table 1 Experimental results obtained for D=(350 2) mm y Act=(5° 2 ). x is the axial translation and Xe is the experimental value obtained from Eq. (1).
Echo directivity was experimentally studied for surface SH Wave probes and SH Wave angle probes. Frequencies used in the experiment were 5MHz and 2MHz, the angles of refraction 90°and 70°, the crystal size 10X 10mm and 5X5mm. The echo directivity was evaluated, using side drilled holes of various depths. The experimental results showed consistency with the calculation based on a point sound source assumption on the test surface in different phases. [Pg.902]

Fig. 3 and 4 show the comparison of the experimental results with the calculation. The symbol O is the result of 03.0mm drilled hole. The symbol is the result of 01.5 mm drilled hole. Fig. 3 shows the strong directivity on and near the surface. [Pg.903]

Fig. III-3. Comparison of Eq. III-18 (solid line) with experimental results for cyclohexane bridges formed between crossed mica cylinders the dashed line is the calculation including Eq. III-20 (from Ref. 19). Fig. III-3. Comparison of Eq. III-18 (solid line) with experimental results for cyclohexane bridges formed between crossed mica cylinders the dashed line is the calculation including Eq. III-20 (from Ref. 19).
Barnes and Hunter [290] have measured the evaporation resistance across octadecanol monolayers as a function of temperature to test the appropriateness of several models. The experimental results agreed with three theories the energy barrier theory, the density fluctuation theory, and the accessible area theory. A plot of the resistance times the square root of the temperature against the area per molecule should collapse the data for all temperatures and pressures as shown in Fig. IV-25. A similar temperature study on octadecylurea monolayers showed agreement with only the accessible area model [291]. [Pg.148]

Figure Al.6.7. Schematic diagram illustrating the different possibilities of interference between a pair of wavepackets, as described in the text. The diagram illustrates the role of phase ((a) and (c)), as well as the role of time delay (b). These cases provide the interpretation for the experimental results shown in figure Al.6.8. Reprinted from [22],... Figure Al.6.7. Schematic diagram illustrating the different possibilities of interference between a pair of wavepackets, as described in the text. The diagram illustrates the role of phase ((a) and (c)), as well as the role of time delay (b). These cases provide the interpretation for the experimental results shown in figure Al.6.8. Reprinted from [22],...
Figure Al.6,8 shows the experimental results of Scherer et al of excitation of I2 using pairs of phase locked pulses. By the use of heterodyne detection, those authors were able to measure just the mterference contribution to the total excited-state fluorescence (i.e. the difference in excited-state population from the two units of population which would be prepared if there were no interference). The basic qualitative dependence on time delay and phase is the same as that predicted by the hannonic model significant interference is observed only at multiples of the excited-state vibrational frequency, and the relative phase of the two pulses detennines whether that interference is constructive or destructive. Figure Al.6,8 shows the experimental results of Scherer et al of excitation of I2 using pairs of phase locked pulses. By the use of heterodyne detection, those authors were able to measure just the mterference contribution to the total excited-state fluorescence (i.e. the difference in excited-state population from the two units of population which would be prepared if there were no interference). The basic qualitative dependence on time delay and phase is the same as that predicted by the hannonic model significant interference is observed only at multiples of the excited-state vibrational frequency, and the relative phase of the two pulses detennines whether that interference is constructive or destructive.
The next few sections deal with the way these experimental results can be developed into a mathematical system. A reader prepared to accept the second law on faith, and who is interested primarily in applications, may skip section A2.1.4.2 and section A2.1.4.6 and perhaps even A2.1.4.7. and go to the final statement in section A2.1.4.8. [Pg.333]

Given this experimental result, it is plausible to assume (and is easily shown by statistical mechanics) that the chemical potential of a substance with partial pressure p. in an ideal-gas mixture is equal to that in the one-component ideal gas at pressure p = p. [Pg.358]

As we have seen, the third law of thermodynamics is closely tied to a statistical view of entropy. It is hard to discuss its implications from the exclusively macroscopic view of classical themiodynamics, but the problems become almost trivial when the molecular view of statistical themiodynamics is introduced. Guggenlieim (1949) has noted that the usefiihiess of a molecular view is not unique to the situation of substances at low temperatures, that there are other limiting situations where molecular ideas are helpfid in interpreting general experimental results ... [Pg.374]

Substances at high dilution, e.g. a gas at low pressure or a solute in dilute solution, show simple behaviour. The ideal-gas law and Henry s law for dilute solutions antedate the development of the fonualism of classical themiodynamics. Earlier sections in this article have shown how these experimental laws lead to simple dieniiodynamic equations, but these results are added to therniodynaniics they are not part of the fonualism. Simple molecular theories, even if they are not always recognized as statistical mechanics, e.g. the kinetic theory of gases , make the experimental results seem trivially obvious. [Pg.374]

These results do not agree with experimental results. At room temperature, while the translational motion of diatomic molecules may be treated classically, the rotation and vibration have quantum attributes. In addition, quantum mechanically one should also consider the electronic degrees of freedom. However, typical electronic excitation energies are very large compared to k T (they are of the order of a few electronvolts, and 1 eV corresponds to 10 000 K). Such internal degrees of freedom are considered frozen, and an electronic cloud in a diatomic molecule is assumed to be in its ground state f with degeneracy g. The two nuclei A and... [Pg.405]

The Debye-Htickel limiting law predicts a square-root dependence on the ionic strength/= MTLcz of the logarithm of the mean activity coefficient (log y ), tire heat of dilution (E /VI) and the excess volume it is considered to be an exact expression for the behaviour of an electrolyte at infinite dilution. Some experimental results for the activity coefficients and heats of dilution are shown in figure A2.3.11 for aqueous solutions of NaCl and ZnSO at 25°C the results are typical of the observations for 1-1 (e.g.NaCl) and 2-2 (e.g. ZnSO ) aqueous electrolyte solutions at this temperature. [Pg.488]

Figure A2.4.5. Theoretical variation of the activity coefficient with Tfroin equation (A2.4.61) and experimental results for 1-1 electrolytes at 25°C. From [7],... Figure A2.4.5. Theoretical variation of the activity coefficient with Tfroin equation (A2.4.61) and experimental results for 1-1 electrolytes at 25°C. From [7],...
Figrne A2.5.23 reproduees Guggeitiieim s figure, with experimental results and the fit to equation (A2.5.25). [Pg.640]

Most of the theoretical predictions have now been substantially verified by a large series of experiments in a number of laboratories. Knobler and Scott and their coworkers (1977-1991) have studied a number of quasibinary mixtures, in particular ethane + (liexadecane + octadecane) for which the experimental n.2 = 17.6. Their experimental results essentially confimi the theoretical predictions shown in figure A2.5.31. [Pg.660]


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