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Adsorption data, lead

Mechanisms of Sorption Processes. Kinetic studies are valuable for hypothesizing mechanisms of reactions in homogeneous solution, but the interpretation of kinetic data for sorption processes is more difficult. Recently it has been shown that the mechanisms of very fast adsorption reactions may be interpreted from the results of chemical relaxation studies (25-27). Yasunaga and Ikeda (Chapter 12) summarize recent studies that have utilized relaxation techniques to examine the adsorption of cations and anions on hydrous oxide and aluminosilicate surfaces. Hayes and Leckie (Chapter 7) present new interpretations for the mechanism of lead ion adsorption by goethite. In both papers it is concluded that the kinetic and equilibrium adsorption data are consistent with the rate relationships derived from an interfacial model in which metal ions are located nearer to the surface than adsorbed counterions. [Pg.6]

In the following section, it is shown that mathematical methods which have been used to interpret adsorption data bias the interpretation towards chemical and electrostatic properties which lead to a significantly sub-Nernstian response this bias arises out of the need for mathematical simplifications, not from physical considerations. [Pg.68]

Precipitation of Hafnium Hydroxide. In order to interpret the adsorption data it was necessary to determine the conditions which lead to the precipitation of hafnium hydroxide. It is not usually advisable to depend on the solubility product because the information on this quantity is often unreliable for hydroxides of polyvalent metal ions. In addition, "radiocolloids may apparently form much below saturation conditions in radioactive isotope solutions. In the specific case of hafnium hydroxide only two measurements of the solubility seem to have been reported. According to Larson and Gammill (16) K8 = [Hf(OH)22+] [OH ]2 — 4 X 10"26 assuming the existence of only one hydrolyzed species Hf(OH)22+. The second reported value is Kso = [Hf4+] [OH-]4 = 3.7 X 10 55 (15). If one uses the solubility data by Larson and Gammill (Ref. 16, Tables I and III) and takes into consideration all monomeric hafnium species (23) a KBO value of 4 X 10 58 is calculated. [Pg.57]

The resemblance of the photocurrent to the optical adsorption spectrum has suggested the involvement of molecular excited states in the creation of charge carriers. While this resemblance is by no means universally observed, the concept of carrier creation via exciton interactions at or very near the illuminated electrode has become increasingly favored. Many of the data leading to these conclusions have been obtained by the use of pulsed light techniques (6, 7,3). These methods are virtually independent of electrode effects and the subsequent analysis of the transient current has led to considerable advances in the theory of charge transfer in molecular crystals. [Pg.332]

Adsorption may lead to an increase or decrease in titrable groups. Titration data can thus be interpreted in terms of conformational changes. [Pg.33]

The reversibility of the adsorption steps in mechanism (4) affects the total number of steady states. As can be seen from Table 1, if two adsorption steps are reversible, boundary steady-state points are absent. Irreversibility of one adsorption step leads to the appearance of one boundary steady-state point in which the concentration of the reversibly adsorbing substance is equal to zero and the irreversibly adsorbing substance occupies all active sites of the catalyst surface. In the case where both adsorption steps are irreversible, there exist two boundary steady-state points (x = 0, y = C2) and (x = Cz, y = 0). In the latter case, at equal kinetic orders of the adsorption steps (n = m) a multiplicity of steady-state solutions is possible, i.e. at pk2 = qk1 (non-rough case) there exists a singular line of steady states connecting two boundary steady-state points. It can manifest itself in the unreproducibility of experimental data in a certain range of the parameters. [Pg.274]

A reaction sequence analogous to that in Eq. 4.40 can also be developed for the specific adsorption of bivalent metal cations (e.g., Cu2+, Mn2 or Pb2+) by metal oxyhydroxides.21 In this application the abstract scenario in the first row of Table 4.3 is realized with A = =Al-OH, B = M2+, C = =Al-OH - - M2+, D = = Al-OM+, and E = H where M is the metal complexed by an OH group on the surface of an aluminum oxyhydroxide. Analysis of pressure-pulse relaxation kinetics data leads to a calculation of the second-order rate coefficient kf, under the assumption that the first step in the sequence in Eq. 4.40 is rate determining. Like k(l, the rate coefficient for the dissolution of a metal-containing solid (Section 3.1 cf. Fig. 3.4), measured values of k, correlate positively in a log log plot with kw,. , the rate coefficient for water exchange on the metal... [Pg.155]

Figure 5. Comparison of lead adsorption data (points and solid connecting lines) with best-fitting James-Healy model predictions (broken lines)... Figure 5. Comparison of lead adsorption data (points and solid connecting lines) with best-fitting James-Healy model predictions (broken lines)...
The first of these tests requires adsorption data on the three binary pairs that can be made from the liquids 1, 2 and 3. that must be all miscible in all proportions. Many theoretical pictures (see sec. 2.4, particularly [2.4.321) lead to exchange constants K of the form... [Pg.177]

The capacity for the second and third steps are reduced and unchanged, respectively, compared to MCM-22. The adsorption data suggest that pillaring leading to MCM-36 increases accessibility of one kind of pores while others (most likely the 10-member channels) are unaffected. The combination of MCM-22 layers with a pillared structure results in a unique hybrid of micro- and mesoporosity, which should lead to interesting applications. [Pg.308]

Reference data for the adsorption of benzene, dichloromethane and methanol have been used to construct as plots for the adsorption of these vapoius on Carbosieve, Takeda molecular sieve carbons, Maxsorb superactivated carbons and a charcoal cloth. It is shown that the as method can give satisfactory results when applied to organic adsorptives provided that good quality adsorption data at higher pressures is available. It is also shown how analysis of the as plots can lead to useful information about the pore structure of the different types of carbon, and some of the difficulties associated with the use of nitrogen adsorption at 77K for the characterisation of microporous carbons are discussed. [Pg.323]

This paper aims at presenting the results of the potential theory applied to high pressure and high temperature adsorption data for both sub and supercritical fluids. We used two different procedures for the calculation of the reference characteristic curve The first one is based on the works by Ozawa, Agarwal and Dubinin The second one is based on the works by Dhima and Neimark. The second method leads to satisfactory results as it is possible to obtain a unique characteristic curve but it requires the revision of the classical laws relating the characteristic curve to the structural properties of the adsorbent Using this procedure, it has been possible to point out the influence of the buoyancy effect on the adsorbed phase for the high pressure data and to propose a method to correct it... [Pg.333]

Sorption phenomena are well described and documented in the basic scientific hterature [1] and standard physical chemistry texts [2-4]. Indoor air researchers first reported extensively on adsorption to and desorption from indoor surfaces in 1987 at the 4th International Conference on Indoor Air Quahty and Climate in Berlin where Seifert and Schmal [5] reported the sink effects of plywood and carpet exposed to lindane and a mixture of 20 volatile organic compounds (VOCs). The Berlin conference also provided data from two studies that examined the sink effect of textiles [6,7]. Finally, Skov and Valbjorn [8] reported on the seminal Danish town hall study. They concluded that sorption to and from large surface areas and fleecy materials was associated with lAQ problems. This work was followed up by Nielsen [9] at Healthy Buildings 88 in Stockholm, where he reviewed several studies on the importance of sorption processes on lAQ. Also in Stockholm, Berglund and her colleagues [10] provided an extensive hterature review and discussion of lAQ data leading to the conclusion that sink effects are important. They also provided the results of a study on adsorption and desorption in a ventilation system. Since then, numerous overviews have been presented on the importance of sink effects on lAQ [11,12]. [Pg.74]

We have analyzed here a variety of adsorption data obtained while investigating the adsorption at oxide/water vapour interface, and oxide/electrolyte interface. That analysis summarized our extensive research conducted during the past few years, and concerning the model of adsorption on oxide surfaces. Our analysis shows, that only the model of energetically heterogeneous surface can be a proper basis for a successful theoretical description of adsorption at water vapour/oxide, and oxide/electrolyte interfaces. It is also demonstrated, that a simultaneous analysis of adsorption isotherms and heats of adsorption may lead to a new level of understanding the mechanism of adsorption in those systems. [Pg.405]

For proton adsorption on well studied systems intrinsic affinity distributions can be obtained after conversion of the (T5(pH) curves into curves using the SGC model with a reasonable value for Ci,t. As indicated before the adequacy of the applied double layer model can be checked when adsorption data are available at a series of indifferent electrolyte concentrations. Replotting the surface charge as a function of pHs should lead to merging of the individual curves into a master curve [44, 45]. The master curve reflects the chemical heterogeneity [46-48]. [Pg.790]

For common adsorbates the equilibrium constants of reactions involving only solution species are available from literature for less common adsorbates they can be determined in separate experiments that do not involve the adsorbent. The equilibrium constants of (hypothetical) surface reactions are the adjustable parameters of the model, and they are determined from the adsorption data by means of appropriate fitting procedure. With simple models (e.g. the model leading to Langmuir equation which has two adjustable parameters) the analytical equations exist for least-square best-fit model parameters as the function of directly measured quantities, but more complicated models require numerical methods to calculate their parameters. [Pg.586]

If appreciable precipitation occurs, however, it leads to erroneous adsorption data—as we have noted in several cases. The problem is obviously more serious with the higher equivalent weight surfactants (Eq. wt. > 400) and these are the surfactants of greatest interest for improved oil recovery by micellar flooding. [Pg.16]


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See also in sourсe #XX -- [ Pg.249 , Pg.250 , Pg.253 ]




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Lead adsorption

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