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Adsorption enthalpy isothermal

Enthalpy of displacement isotherms were determined by the flow technique. The heat effects recorded on dodecylammonium and dodecyldiammonium ver-miculites are found to be endothermic in both cases, i.e., the measured heat exchange process results in heat extraction. Since the adsorption isotherms unambiguously indicate positive adsorption of n-butanol, the question arises as to why an exothermic exchange enthalpy is not recorded. In our opinion, the reason for this is the endothermic enthalpy of dilution [59-61,69], which overcompensates for the interlamellar adsorption of butanol. When, knowing the adsorption excesses, the enthalpy isotherm A21// = f Xy,) characteristic of the solid/Uquid interfacial adsorption layer can be calculated, it is indeed the exothermic adsorption enthalpy isotherm specific for the surfacial interaction that is obtained (Fig. 30). This measurement suggests that the interlamellar adsorption of n-butanol is thermodynamically preferred and is accompanied by the liberation of a very large amount of heat (A21// = 16.0-16.5 J/g). [Pg.396]

It is not necessary to limit the model to idealized sites Everett [5] has extended the treatment by incorporating surface activity coefficients as corrections to N and N2. The adsorption enthalpy can be calculated from the temperature dependence of the adsorption isotherm [6]. If the solution is taken to be ideal, then... [Pg.392]

In the gas-phase chromatography experiments, the measure of volatility is assumed to be either a deposition temperature in a thermochromatography column or the temperature in an (isothermal) column at which 50% (T50%) of the desired product (50% chemical yield ) are passing through the gas chromatography column [8]. The values are then correlated with the adsorption enthalpies (AHads). The latter is then related to the sublimation enthalpy (AHsub), a property of the macro-amount using some models, see... [Pg.64]

Fig. 20. Yield curves vs. isothermal temperature measured for oxychloride compounds of the nuclides 108Tc (A), 169Re ( ), 218Po ( ), and 218Bi ( ) in the chemical system He(g)/02(g)/HCl(g)/Si02(S). The dotted lines indicate the results of simulations with the microscopic model of Zvara [47] with the adsorption enthalpies indicated. Figure reproduced from [54] with the permission of Oldenbourg Verlag. Fig. 20. Yield curves vs. isothermal temperature measured for oxychloride compounds of the nuclides 108Tc (A), 169Re ( ), 218Po ( ), and 218Bi ( ) in the chemical system He(g)/02(g)/HCl(g)/Si02(S). The dotted lines indicate the results of simulations with the microscopic model of Zvara [47] with the adsorption enthalpies indicated. Figure reproduced from [54] with the permission of Oldenbourg Verlag.
Fig. 22. Relative yields of the compounds l08TcO3Cl (O), 169Re03Cl ( ), and (most likely) 267Bh03Cl ( ) as a function of isothermal temperature. The error bars indicate a 68% confidence interval. The solid lines indicate the results of simulations with the microscopic model of I. Zvara [18] with the adsorption enthalpies given in the text. The dashed lines represent the calculated relative yield concerning the 68% confidence interval of the standard adsorption enthalpy of Bh03Cl from -66 to -81 kJ/mol. Figure reproduced from [55],... Fig. 22. Relative yields of the compounds l08TcO3Cl (O), 169Re03Cl ( ), and (most likely) 267Bh03Cl ( ) as a function of isothermal temperature. The error bars indicate a 68% confidence interval. The solid lines indicate the results of simulations with the microscopic model of I. Zvara [18] with the adsorption enthalpies given in the text. The dashed lines represent the calculated relative yield concerning the 68% confidence interval of the standard adsorption enthalpy of Bh03Cl from -66 to -81 kJ/mol. Figure reproduced from [55],...
As noted above, many investigations have been made of the adsorption of water on non-porous silicas. Less attention has been given to the dehydroxylation of porous silicas. An early study by Dzhigit et al. (1962) of the adsorption water vapour on a mesoporous silica gel involved both isotherm and calorimetric measurements. It was found that at very low surface coverage the adsorption enthalpy was not significantly affected by dehydroxylation, but a large difference became apparent as the surface coverage increased. A slow uptake of water vapour, which occurred after dehydroxylation, was attributed to chemisorption. [Pg.310]

Flfure 2.28. Adsorption of long-chain alkanes from n-heptane on various grades of graphite, (a, left). Enthalpy isotherms for n-docosane (n-CjjH g) (a, right), correlation with the enthalpy of adsorption for a reference sample (b) adsorption Isotherms for four alkanes on Vulcan 3G. (Redrawn from H.E. Kem, G.H. Findenegg, J. Colloid Interface Set 75 (1980) 346.)... [Pg.223]

The isotherm fields measured could be described with sufficient accuracy by using a modified Langmuir isotherm model, considering the dependence of adsorption enthalpy and adsorption entropy on ACC loading [4]. [Pg.511]

Pursuing more realistic formulae for calculation of the adsorption enthalpy, we will incorporate the mixed adsorption entropy S /R. From Eqs. 5.42 and 5.70 it follows that the entropy change for the each partial adsorption isotherm is ... [Pg.170]

The integral exchange enthalpy isotherm calculated from the flow microcalorimetric measurements is shown in Fig. 12. The course of the isotherm - in case of a U-shaped adsorption excess isotherm - is determined by the composition of the interfacial phase ( ) according to the following equation[45-47] ... [Pg.889]

One, called isosteric (because, for gas adsorption, it requires comparing two states with same amount adsorbed, i.e., same volume adsorbed), is the calculation of the differential adsorption enthalpy by using a set of two (or, better, three) adsorption isotherms at different temperatures. In dilute solution, the calculation of the isosteric enthalpy from adsorption isotherms at different temperatures is done by applying the following equation ... [Pg.293]

The different values of m in equation (10.21) are attributed to the different pore structures of the adsorbents. The adsorption enthalpies, calculated using the DA isotherm, remain below 5 kJ/mol as a function of adsorbed density (within the range of validity of the Dubinin model), consistent with physisorption. [Pg.280]

The Freundlich isotherm is valid at low coverage. The adsorption enthalpy depends on coverage as ... [Pg.297]

An international group (Gaggeler et al., 1992 Tiirler, 1992) used OLGA II and 35-s 262Db to perform the first online isothermal gas chromatography of the bromides of element 105. The volatile species were deposited on a moving tape and transported in front of six large area passivated implanted planar Si detectors for measurement of a-particles and SFs. The adsorption enthalpies were nearly... [Pg.353]

In a later experiment (Tiirler et al., 1999), the isothermal temperature was varied to obtain the adsorption enthalpy for Sg. The yield of short-lived W isotopes from reactions on Gd incorporated in the target was also measured at the same time. An adsorption enthalphy of-96 1 kJ mol 1 was obtained for the dioxydichloride of W in agreement with the previous measurement. Based on 11 events attributable to Sg, an adsorption enthalpy of -100 4 kJ mol-1 or 96 1 kJ mol 1 was obtained depending on the Sg half-life used in the Monte Carlo calculations. Thus, the experimental results confirmed the theoretically predicted volatility sequence of Mo > W > Sg. From an analysis of the decay properties of the correlated decay chains detected in these experiments, Tiirler et al. (1998) were able to recommend better half-lives and cross sections of 7.4 + 3.3/ - 2.7 s and approximately 0.24 nb for 265Sg and of 21 + 20/ - 12 s and approximately 0.025 nb for 266Sg for 22Ne beam energies between 120 and 124 MeV. [Pg.355]

The dynamic nature of the frameworks in MIL-53 (Cr and Al) also results in very interesting CO2 and CH4 adsorption behaviours (Fig. 11) [133]. CH4 adsorption isotherms for MIL-53 are typical of those obtained with microporous materials such as zeolites and activated carbon. At 35 bar and 304 K, the amount adsorbed is 155 (Al) and 165 (Cr) v(STP)/v. The adsorption enthalpy of CH4 remains almost constant at 17 kJ moP from 0 to 10 bar, which is well above the liquefaction enthalpy of CH4 (8.2 kJ moP ). The maximum CO2 adsorption is 10 mmol g for MIL-53(A1), observed at 304 K and 30 bar. This is a moderate capacity however, the shape of the CO2 adsorption isotherm is very unusual and shows a first adsorption step below 1 bar adsorbing 2 mmol g CO2, followed by a second adsorption step at around 6 bar. Interestingly, no steps were found to be present in the CO2 desorption process. The corresponding adsorption enthalpy for CO2 on MIL-53(A1) is around 35 kJ moP during the initial adsorption process up to 6 bar, which is followed by a sharp decrease to around 17 kJ moP close to the liquefaction enthalpy of CO2 (17.2 kJ moP ). MIL-53(Cr) exhibits similar behaviour in CO2 adsorption the first step in CO2 adsorption in dehydrated MIL-53(Cr) disappears if the sample is hydrated [135]. For hydrated MIL-53(Cr) CO2... [Pg.55]


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