Alexey V. Nabok, Aseel K. Hassan and Asim K. Ray*
Electronic Research Group, School of Engineering, Sheffield Hallam University, Pond Street, Sheffield, UK S1 1WB
First published on UnassignedUnassigned22nd December 1999
Adsorption of vapours of benzene, toluene, p-xylene, aniline, hexane and chloroform in LB films of two novel calix[4]resorcinarene derivatives was studied in situ using quartz-crystal microbalance (QCM), ellipsometry and surface plasmon resonance (SPR) techniques. Isotherms of adsorption obtained by both QCM and SPR show that the adsorption ability depends on the condensed vapour pressures of the adsorbates rather than on a structural coincidence between host cavities and guest molecules. The results were interpreted in terms of capillary condensation of organic vapours in the nanoporous matrix of calixarene LB films accompanied by film swelling. Ellipsometric measurements show changes of both the thickness and refractive index of the LB films caused by adsorption, and thus confirm condensation and further accumulation of liquid adsorbate within the film matrix. Unusual adsorption kinetics were observed only when the vapour injection technique was used and their occurrence is believed to be caused by initial vapour condensation on the film surface. This can be eliminated by measurements under constant vapour flow.
Several attempts to study the adsorption of organic vapours within thin calixarene films formed with different techniques, including LB film deposition, spin coating and self-assembly, have been made. 16–22 In recent publications 21,22 we have shown that the vapours of benzene and toluene, as well as some hydrocarbons (hexane), can be adsorbed at calixarene Langmuir–Blodgett (LB) films. This adsorption process is very fast, and full recovery of the film has been observed after flushing with clean air. It has to be pointed out, however, that the detected vapours were of a high concentration (a few percent in volume) and the adsorption was not selective since all vapours studied yielded a similar response. These effects are attributed to weak and non-specific interactions between guest molecules and the calixarene LB film. It was also shown that the adsorption of organic vapours occurs in the whole bulk of the LB films, and that the number of adsorbed molecules is much higher than the number of calixarene molecules. 21 The proposed mechanism of adsorption included swelling of the film and even condensation of adsorbate within the film. The swelling of the film has been confirmed directly by ellipsometry and surface plasmon resonance (SPR) measurements. 21,22 but the mechanism of adsorption is still unclear.
Different calix[4]resorcinarene derivatives have been deposited by self-assembly and spin-coating techniques onto QCM and SAW devices, and their response to various organic vapours has been studied. 23 Although a few particular calixarene–vapour combinations have shown a high selective host–guest type molecular recognition, the majority of calixarene compounds have resulted in a more or less similar response to different organic vapours. It seems that the cavitand nature of sensing molecules is not necessary for this mechanism of adsorption, since a similar effect has been observed in phthalocyanine LB films in response to their exposure to toluene vapours. 24
The presence of alkyl chains is important for this type of complexation. All the organic guests investigated are solvents in the liquid phase, and they can therefore interact with the alkyl chains of amphiphilic calixarene derivatives. This has been proved by NMR spectral measurements of the complexation of toluene with phosphorylated calix[4]resorcinarenes. 25 In contrast, thin films of unsubstituted calix[ n]arenes, produced by vacuum evaporation, show a permanent binding of benzene derivatives, possibly, due to the formation of inclusion complexes. 26
In our previous study of the adsorption kinetics using ellipsometry and SPR, an initial sharp response on vapour injection followed by a decay and stabilisation has been recorded. 21,22 It was suggested that such unusual adsorption kinetics could be attributed either to formation of liquid state adsorbate on the film surface or to some possible experimental artefacts.
Taking into consideration all known experimental facts, we can assume a more complex adsorption mechanism. This includes, in addition to the conventional host–guest binding within calixarene cavities, the interaction of guest molecules with alkyl chains, their penetration into the film bulk through pores, as well as their further condensation inside the film in a liquid state. In order to prove this mechanism, the adsorption of different organic molecules such as aromatic compounds (benzene, toluene, p-xylene, etc.), hydrocarbons (hexane) and chloro-hydrocarbons (chloroform), in LB films of several calixarene derivatives was studied using a number of methods including QCM, ellipsometry, and SPR.
Two amphiphilic calix[4]resorcinarene derivatives were used in the present study. These are phosphorylated and azobenzene substituted compounds, referred to throughout the text as P-C[4]RA and Azo-C[4]RA, respectively. The chemical structures of these compounds are shown in Fig. 1. The synthesis of these calixarene derivatives has been described previously. 25,27 P-C[4]RA molecule has a boat-like conformation, 25 while Azo-C[4]RA forms a cone with the cavity extended by the presence of four azobenzene groups. 27 The difference in the shape of these two compounds may cause variation in their adsorption properties.
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Fig. 1 Chemical structures of (a) P-C[4]RA and (b) Azo-C[4]RA derivatives. |
The QCM set-up, consisting of an electrical oscillating circuit and a gas chamber, was made in-house. Certain concentrations of odorant vapours, in particular toluene and hexane, were prepared within the chamber by injecting the required amount of liquid toluene and hexane. The frequency of the quartz oscillator (which was in the range 10–11 MHz) was monitored using a frequency-counter, and readings were taken twice before an exposure and under steady state conditions, when evaporation of the liquid droplet within the chamber was complete and the equilibrium vapour concentration had been formed.
Ellipsometric measurements were carried out using a zero-type LEF 3M instrument equipped with HeNe (632.8 nm) laser source and a specially designed gas cell described previously. 21 Both polariser and analyser were fixed at positions (angles) of P0 and A0, respectively, providing the minimum of the output light intensity. Initial values of the thickness ( d) and refractive index ( n) of the film were calculated from P0 and A0. In order to follow the adsorption kinetics, the photodetector output signal was monitored on a chart-recorder during the injection of vapour into the gas cell. When steady state adsorption was reached, a new set of readings ( A1, P1) were taken and new values of d and n were calculated. Certain concentrations of vapour were achieved by diluting saturated vapour with air.
SPR measurements were carried out using the Kretschmann type θ–2 θ rotated stage experimental set-up described previously. 22 The samples were brought into optical contact with the equilateral prism using an index-matching liquid (ethyl salicylate from Aldrich). A p-polarised HeNe laser beam ( λ = 632.8 nm) was used for excitation of surface plasmons. A gas cell, sealed at the sample through a rubber O-ring, was used to study vapour adsorption in the calixarene LB films. Kinetic SPR measurements of the intensity of reflected light at the fixed angle θ*, chosen near the SPR minimum on the left side of the SPR curve, were performed in situ during exposure to organic vapour.
In order to study the adsorption kinetics in detail, three methods of vapour preparation were employed in the SPR measurements: (i) injection of vapours at a certain concentration, prepared by dilution of the saturated vapours, into the gas cell; (ii) injection of a small amount of liquid solvent into the gas cell and the slow formation of the saturated vapour during its evaporation; and (iii) measurements in a constant vapour flow. A Standard Vapour Generator (A.I.D. model 350) was used in the latter case. The vapour concentration was calculated for a particular solvent at a certain temperature, knowing the geometrical dimensions of the diffusion sample tube used. 28
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where f0 (10–11 MHz) is the nominal frequency of quartz crystals. This formula was derived from the Sauerbrey equation, 29 based upon an ideal mass approach and valid for thin films causing frequency changes not more than 1% of its nominal value. The concentration of adsorbed guest molecules Nads can be calculated from eqn. (2).
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where NA is Avogadro's number, A is the area of the quartz crystal, d is the thickness of LB coating and M = 92 and 84, the molecular weights of toluene and hexane, respectively. Knowing the concentration of calixarene molecules in the LB films, one can calculate the number of adsorbed guest molecules per calixarene moiety.
Fig. 2 shows typical results obtained by QCM measurements on quartz crystals coated with LB films (30 layers) of P-C[4]RA when exposed to toluene and hexane vapour of various concentrations. The mass gain was found to increase monotonically with increasing vapour concentration up to a saturation level, indicating a bulk adsorption mechanism. It can be also seen from Fig. 2 that the adsorption of toluene vapour is more efficient than hexane. The number of adsorbed molecules per calixarene unit was found to be about 10 for hexane and 20 for toluene at the pressure of 0.9 PS. This corresponds well to the results obtained previously on the adsorption of benzene in C[4]RA LB films. 21 The numbers of adsorbed molecules found are much greater than those expected from the geometrical dimensions of the intrinsic calixarene cavity and the empty space between molecules. In order to explain this discrepancy, we have to assume either film swelling or condensation of vapour inside the film or both.
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Fig. 2 The results of QCM measurements of P-C[4]RA LB films (20 layers) on exposure to toluene and hexane vapour of various concentrations. |
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Fig. 3 The kinetics of the photodetector signal in ellipsometric measurements on P-C[4]RA LB films (20 layers) in response to injection of hexane vapour. |
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by using a least-squares fitting technique. In the above equation, Ψ and Δ are, respectively, the amplitude ratio and the phase shift of p- and s- components of polarised light reflected from the film surface. Reasonably thick LB films (20 layers) were used in these experiments in order to avoid thicknesses less than 10 nm, which leads to very poor resolution for the simultaneous determination of both n and d. A value of k = 0 for the extinction coefficient was used for these calculations since calixarene films are transparent at 632.8 nm.
The initial n and d values for P-C[4]RA LB films were found to be of 1.46 and 13.8 nm, respectively, which corresponds well to the results obtained previously for the LB films of unmodified C[4]RA. 21
Fig. 4 shows the changes of both the thickness and refractive index of LB films of P-C[4]RA in response to toluene and hexane vapours of various concentrations. The film thickness was found to increase monotonically with the vapour concentration confirming the assumption of film swelling. However, relative changes of the thickness, falling in the range of 10%, are still not enough to provide the room required for a few tens of guest molecules per one calixarene unit. Condensation of vapour inside the film should, therefore, be taken into consideration.
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Fig. 4 The dependences of the optical parameters of P-C[4]RA LB films (20 layers) on the concentration of toluene and hexane vapours: (a) refractive index, (b) film thickness. |
As seen from Fig. 4, adsorption of toluene results in an increase of n from 1.46 (for unexposed LB film) to 1.49 on exposure to a nearly saturated vapour pressure. On the contrary, exposure to hexane vapour leads to a decrease in n value down to 1.43 at saturated pressure level. These results can be explained in terms of accumulation of liquid solvents within the film bulk. In the case of liquid toluene having n = 1.49, the effective refractive index of the film increases from its initial value 1.46 with an increase of toluene content. In contrast, accumulation of liquid hexane ( n = 1.37) leads to a decrease in the effective n value for calixarene LB films.
Similar results have been obtained recently on thin films of poly(dimethylsiloxane) using spectroscopic ellipsometry. 31 It has been found that exposure of the films to tetrachloroethane and toluene vapours causes an increase in refractive index, while cyclohexane, having n similar to that of the polymer, did not produce any significant changes.
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Fig. 5 The kinetics of SPR response of Azo-C[4]RA LB films (4 layers) to benzene vapour of various concentrations: 1) pS, 2) pS/10, 3) pS/100, 4) pS/1000, 5) pS/10000. |
The values of the response for different vapours (in the form of relative changes of the reflected light intensity), corresponding to steady state conditions, are summarised in Fig. 6. Two important features of the adsorption isotherms presented in Fig. 6 should be identified. Firstly, all isotherms show Langmuir adsorption (typical of thin films of absorbent 32) over a wide range of concentrations up to 0.1 pS (with pS the saturated vapour pressure) with a sharp increase of the response at pressures of about 0.2 pS. The latter can be attributed to an effect similar to capillary condensation in porous absorbents. 32 Secondly, the relative response correlates well with the saturated vapour pressure ( pS) of the vapours studied in the following sequence: chloroform ( pS = 190 mmHg), hexane (160 mmHg), benzene (75 mmHg), toluene (20 mmHg), p-xylene (3 mmHg), aniline (< 0.5 mmHg).
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Fig. 6 Isotherms of adsorption of different organic vapours in Azo-C[4]RA LB films obtained with SPR. |
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where p and pS are the saturated vapour pressure inside the capillaries with a radius r and in normal conditions, respectively. V is the molar volume and γ is the surface tension of the adsorbate and θ is the wetting angle in the capillary. This model can be extended to the case of nanoporous systems like the calixarene LB films with a characteristic pore size of about 1 nm. Knowing the parameters V and γ for particular adsorbates at room temperature and assuming full wetting of the pores by the solvents ( θ = 0), one can estimate p as 0.2–0.3 pS. This means that condensation of solvent vapours in calixarene LB films may start at pressures of about 0.2 pS, what is exactly observed in the current experiment (see Fig. 6).
The observed correlation between the values of the relative response and saturated vapour pressure becomes more understandable now, since more volatile solvents, having higher pS, will be condensed more easily. From this point of view, measuring vapour concentration in pS units seems to be more appropriate than in absolute values such as ppm. Simple calculations, based on an ideal gas approach, show for instance, that the saturation vapour of benzene is equivalent to 98000 ppm, compared to 4000 ppm for p-xylene and 800 ppm of aniline.
Since the unusual kinetics were observed only in the case of using the vapour injection technique, two other methods of vapour preparation have been elaborated. Fig. 7 shows the SPR response of an Azo-C[4]RA LB film on exposure to saturated vapours of hexane, chloroform and toluene, formed within a gas cell by evaporation of a small droplet of the corresponding liquid solvent. The opposite type of kinetics observed here can easily be explained by the increasing vapour pressure (up to the saturation level) during the evaporation of liquid solvent. With this method it is difficult to control precisely the amount of injected liquid, which is required to form particular vapour concentrations lower than the saturated value.
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Fig. 7 SPR response on exposure of Azo-C[4]RA LB films (4 layers) to saturated organic vapours formed by evaporation inside the gas cell. |
On the contrary, the method of running a constant vapour flow into the gas cell using a Standard Vapour Generator seems to provide the best option. The results obtained using this technique and presented in Fig. 8 show the absence of kinetics of both types, i.e. the sharp initial peak and the slow and gradual increase of the response. The response to a constant vapour flow is very fast as is the decay of the signal on flushing with a constant flow of nitrogen. A response time of about 10–12 s was found, much higher than a time of about 1 s required to fill the 2.5 cm 3 gas cell under a flow rate of 150 cm 3 min −1. Thus, the characteristic adsorption time constant is of the order of 10 s. It can be concluded therefore that the observed unusual kinetics of the response are due to the method of injection of a highly concentrated vapour. The mechanism of this kind of kinetics is caused, possibly, by the initial vapour condensation on the surface of the calixarene LB film with subsequent diffusion of the adsorbents inside the film matrix.
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Fig. 8 SPR response of Azo-C[4]RA LB films (4 layers) to a constant flow of toluene vapour of concentration of 180 ppm. |
The technique of vapour injection, used in the present study, as well as in our earlier publications, yields an additional sharp initial increase of the response, possibly due to initial vapour condensation on the film surface. The constant vapour flow technique eliminates this unusual kinetic behaviour and consequently would be preferred for further experiments.
Footnote |
† Basis of a presentation given at Materials Chemistry Discussion No. 2, 13–15 September 1999, University of Nottingham, UK. |
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