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Experience curves methanol

J.H model is, indeed, the common behavior. Figure 1 reports the degradation rate of phenol [36], a poorly adsorbed compound, and that of CHBA [35], a strongly absorbed compound, as a function of their initial concentration. A peaked reaction rate is observed, in contrast to the saturative LH model, also for CHCI3 and dodecane (see Fig. 2 in Ref. 37). For the photocurrents measured in photoelectro-chemical oxidation experiments of methanol and salicylic acid on anatase film electrodes, a saturation curve for the poorly adsorbed methanol and a peak at an intermediate concentration for strongly adsorbed salicylic acid were also observed as a function of the substrate concentration [38]. [Pg.217]

Fig. 18.2. First potential scan at a porous platinum electrode in 0.2 M MeOH/O.l M HCI04 starting at 50 mV with 10 mV s 1 (a) current as a function of potential (b) simultaneously recorded mass signal for C02 (mle 44). The lower curves are from a blank experiment without methanol in solution. [From W. Vielstich and X.H. Xia J. Phys. Chem. 99 (1995)... Fig. 18.2. First potential scan at a porous platinum electrode in 0.2 M MeOH/O.l M HCI04 starting at 50 mV with 10 mV s 1 (a) current as a function of potential (b) simultaneously recorded mass signal for C02 (mle 44). The lower curves are from a blank experiment without methanol in solution. [From W. Vielstich and X.H. Xia J. Phys. Chem. 99 (1995)...
The alkali elution curves of the displacement chromatography are shown in Fig. 17, the ratio Li/ Li dependent on the effluent volume is given in Fig. 18. As one can see from Fig. 18, an increase of the Li/ Li ratio from 0.07 to 0.09 is found within the lithium elution band which corresponds to a column length of 91 cm. The relative enrichment of the heavy lithium isotope Li in the first fractions — that is in the methanolic phase — agrees with isotopic separations of calcium using a condensation resin with dibenzo(18]crown-6 and [2b.2.2], respectively (Chap. 4.3.2.3 and Chap. 4.3.2.4). Fujine and coworkers have also carried out one breakthrough experiment with methanolic solutions of cesium chloride and lithium acetate The evaluation of the front analysis with Spedding and coworkers method resulted in an isotopic separation factor of a = 1.014. [Pg.121]

The experience curve for methanol is shown by Figure 6.5. Industry total accumulated production from Figure 6.4 is plotted versus the price in constant... [Pg.202]

What has happened since 1973 to cause the methanol experience curve to be displaced as shown in Figure 6.5 ... [Pg.236]

Divide the experience curve for methanol into spring, summer, autumn, and winter periods of its life cycle. [Pg.236]

Fig. 28.3. Echo attenuation curves in PGSE experiments on methanol adsorbed on organic polymeric resin crosslinked by diamagnetic Cd ions . Fig. 28.3. Echo attenuation curves in PGSE experiments on methanol adsorbed on organic polymeric resin crosslinked by diamagnetic Cd ions .
In their measurements with the cell (195) containing methanol, Non-hebel and Hartley1 verified by direct experiment that the addition of a small drop of water to either side of the cell, sufficient to give a mole fraction of I120 equal to about 0.001, produced a change in the e.m.f. equal to a few millivolts. This was attributed mainly to the proton transfer (44). The curve for HOI in methanol-water mixtures must thus have a very steep slope, as has been sketched on the right-hand side of Fig. 01. [Pg.225]

Figure 7. The Fourier transformed signal AS[r, x] of the (C2H4I) radical in methanol at I = 100 ps. The agreement between theory (red curve) and experiment (black curve) is better if the radical is assumed to be bridged (a) rather than to have an anti form (b). (See color insert.)... Figure 7. The Fourier transformed signal AS[r, x] of the (C2H4I) radical in methanol at I = 100 ps. The agreement between theory (red curve) and experiment (black curve) is better if the radical is assumed to be bridged (a) rather than to have an anti form (b). (See color insert.)...
Figure 2.2 shows also the oxidation pattern of adsorbed methanol in the absence of methanol in the solution (dashed curve). The experiment was performed using the flow cell procedure [36], Methanol was adsorbed from a 10 2 M CF[3OH/0.5 M H2S04 at 250 mV RHE for 10 min, then the solution was exchanged with pure base electrolyte under potential control, and a potential scan was applied. [Pg.139]

In order to check the survival of methanol adsorbate to the transfer conditions, the following experiment was performed. After adsorption of methanol and solution exchange with base electrolyte, the Pt electrode was transferred to the UHV chamber over a period of ca. 10 min, then back to the cell where it was reimmersed into the pure supporting electrolyte. A voltammogram was run and compared with that of an usual flow cell experiment. The results, (see Fig. 2.5a,b), show that the transfer procedure is valid. The areas under the oxidation curve are the same. As in the case of adsorbed CO on Pt (see Fig. 1.4), the change in the double peak structure indicates that some surface re-distribution may occur. [Pg.143]

The current-time response of the system during Sn(Il) addition presents the same features as the mass intensity-time curve. For comparison the i-t curve for a blank experiment (only adsorbed methanol being present, no tin addition) is also shown in Fig. 4.6a. The observed response is not simply the sum of the individual responses of Sn(II) (Fig. 4.2b) and adsorbed methanol (see dashed curve in Fig. 4.6a), to the applied potential step. [Pg.164]

In this experiment, a mixture of methyl, propyl, and butyl paraben (structures shown in Figure 13.14) in methanol solvent will be separated by reverse phase HPLC. Mobile phase compositions of varying polarities will first be tested to see which one gives the optimum resolution of this mixture, and following this, a standard curve for methyl paraben will be constructed and its concentration in this solution determined. [Pg.386]

Fig. 4. Measured transmission versus incident light intensity for solutions of cryptocyanine in glycerol and methanol at room temperature. Initial dye transmission T0 = 1%. Theoretical curves (—) according to Eq. (11a) were obtained from matching theory and experiment at points indicated by arrows. (From Ref. 12))... Fig. 4. Measured transmission versus incident light intensity for solutions of cryptocyanine in glycerol and methanol at room temperature. Initial dye transmission T0 = 1%. Theoretical curves (—) according to Eq. (11a) were obtained from matching theory and experiment at points indicated by arrows. (From Ref. 12))...
To ensure that meaningful results were obtained by C CF MAS NMR spectroscopy, catalytic experiments were performed with a conventional fixed-bed reactor and, under the same conditions, a spinning MAS NMR rotor reactor. The reaction products from both reactors were analyzed by on-line gas chromatography (261). A comparison of the results showed a reasonably good agreement in particular, the methanol conversion takes place in the same temperature range, and the same qualitative behaviors of the conversion and yield curves were found for the two reactors (261). [Pg.213]

In order to find the influence of compression on collapse of the polymer networks, the experiments on the swelling of the deformed gels of AA-SMA in water-methanol and water-dioxane mixtures were performed [29]. It was shown that uniaxial compression of the gel really affects the swelling curves and that, in a good agreement with the theory, the region of stability of the collapsed state increases and the sharpness of collapse decreases under compression. [Pg.158]

Fig. 6. The q-integrated photosignal of iodine in methanol from a time-slicing experiment. The red curve is the temporal profile of the x-ray pulse. Fig. 6. The q-integrated photosignal of iodine in methanol from a time-slicing experiment. The red curve is the temporal profile of the x-ray pulse.
The influence of temperature on the reaction product yield is shown in Figure 4.16. The studies were implemented for a temperature range of 350-475 °C. Hence, values of the remaining parameters were kept identical for all experiments. It is clear from the curves that maximal methanol yield falls within the range of 400-425 °C. Methanol yield decreases with temperature increase, which is explained by recombination of reacting radicals and H202 dissociation rate increase. [Pg.125]

Fig. 1.17 Comparison of theory and experiment for preferential adsorption coefficient, X, of poly(alkyl methacrylate)s in 1,4-dioxane-methanol. (pso = methanol volume fraction). Points Experimental results from ref. [6], (o) PMMA (alkyl = Me) (A) PEMA (Et) ( ) PiBM (iBu). Association equilibria theory. (2-A) Calculated with the parameter values shown in Table I and numbered as 4-6, Curves (a) PMMA (b) PEMA, (c) PiBMA. (2-B) Calculated with the parameter values shown in Table I and numbered as 10-12. Curves (a) PMMA (b) PEMMA (c) PiBMa. (From ref. [120])... Fig. 1.17 Comparison of theory and experiment for preferential adsorption coefficient, X, of poly(alkyl methacrylate)s in 1,4-dioxane-methanol. (pso = methanol volume fraction). Points Experimental results from ref. [6], (o) PMMA (alkyl = Me) (A) PEMA (Et) ( ) PiBM (iBu). Association equilibria theory. (2-A) Calculated with the parameter values shown in Table I and numbered as 4-6, Curves (a) PMMA (b) PEMA, (c) PiBMA. (2-B) Calculated with the parameter values shown in Table I and numbered as 10-12. Curves (a) PMMA (b) PEMMA (c) PiBMa. (From ref. [120])...
Because methanol is not actually a solvent for PVA, some interesting sorption/desorption cycling experiments can be conveniently run on PVA films without disrupting the film integrity. As noted above, methanol produces a slow increase of shear stiffness (Adh) when layered on PVA. The time scale and curve shape are suggestive of a diffusion process (liquid into polymer). By removing the liquid layer, we should permit methanol to evaporate from the film and thus reverse the effect. The... [Pg.171]


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