1 Absract In this work we wanted to underline the importance of Thermal Desorption Spectroscopy and its applications to several branches of Physics. Temperature-programmed desorption techniques (TPD) are important to determinate kinetic and thermodynamic parameters of desorption processes and decomposition reactions. Knowledge of the nature of the desorption process is fundamental to understand the nature of the elementary chemical processes of adsorbates, as the energetics of bonding, the specification of the chemical nature of the bound species and the nature and magnitude of interactional effect between adsorbed species. We focused our attention on the applications of Thermal Desorption Spectroscopy (TDS) to High-Energies Physics, Astrophysics and Geophysics; in fact this technique was used, respectively, to investigate the molecular hydrogen adsorption on carbon nanotubes, the effects of electron bombardment on ammonia and methane ices and changes of zoisite mineral after heating. The molecular hydrogen adsorption on carbon nanotubes was studied to find a possible solution to vacuum system problems of Large Hadron Collider (LHC); in fact, the circular path of photon beams produces synchrotron radiation which deteriorates LHC vacuum desorbing gas molecules from the ring walls. Among the desorbed species the most problematic to pump out is H2. Since LHC elements operate at low temperatures, a possible solution to vacuum problem is the installation of cryosorbent materials on the LHC walls. In this work we study the possibility to use carbon nanotubes as criosorbers in future accelerators. Our sample, furnished by Prof. Nagy group of Chemical Engineering Department of Calabria University, is constituted by MWNTs synthesized by chemical vapor deposition using C2H4 and subsequently purified. Our investigations confirm that the carbon nanotubes have a great adsorption capacity also at low temperatures both for H2 and noble gases as Kr; then we observed that H2 adsorption on CNT is described by a first kinetic-order, while Kr adsorption is characterized by a zero kinetic-order. By means of TDS we calculate the activation energy for H2 adsorption on carbon nanotubes and we found a value of about 3KJ/mol, perfectly coherent with theoretic one. Moreover, from a comparison between nanotubes and other carbon-based material (as charcoal), we noted that adsorption efficiency for CNT is almost an order of magnitude higher then charcoal. So carbon nanotubes are good candidates to cryosorbers in future accelerators. 2 As Thermal Desorption Spectroscopy application to Astrophysics we studied the effect of electron bombardment on ammonia and methane ices. The interstellar medium is composed for 99% by gas; molecules, atoms and radicals at gas state condense on dust grains surface of molecular clouds (at 10 K) creating an icy mantle with a thickness of 0.1 μm. The presence of ices is confirmed by IR spectroscopy of obscured stellar sources and in interstellar grains are localized solid mixture containing H2O, CO, CH4 and NH3. In these environments ices are subjected to chemical and physical processes, specifically to bombardment of photons and cosmic rays, with the consequent synthesis of new organic species In this work we conducted an investigation of the chemical processing of ammonia and methane ices subjected to energetic electrons. By Thermal Desorption Spectroscopy we verify the production of new organic species, after energetic irradiation in interstellar ices, as diazene (N2H2), ethane (C2H6) and acetylene (C2H2). Finally, in Geophysics and Petrology Thermal Desorption Spectroscopy can be used to study minerals chemical composition. Our interest was focused on zoisite and the sample investigated was furnished by prof. Ajò from “Institute of Inorganic Chemistry and Surfaces” of CNR, in Padova. In this work we used TDS to investigate zoisite behaviour during heating form room temperature to 650 o C and to understand if its modification into tanzanite variety after heating is due to structural changes or to a dehydration mechanism. 3 Chapter 1 Thermal desorption spectroscopy 1.1 Adsorption and Desorption fundamental principles Temperature-programmed desorption techniques (TPD) are important to determinate kinetic and thermodynamic parameters of desorption processes and decomposition reactions. Knowledge of the distinctive features is fundamental to understand the nature of the elementary chemical processes of adsorbates, as the energetics of bonding, the specification of the chemical nature of the bound species and the nature and magnitude of interactional effect between adsorbed species[1]. Adsorption takes place when attractive interaction between a particle and a surface is strong enough to overcome thermal disorder effects. Fig. 1.1. Adsorption potential diagram for a diatomic molecule X 2 interacting with a substrate surface along the direction z. Physisorption potential has been described through the Lennard-Jones potential, while chemisorption has been represented by a Morse potential 4 The weakest form of adsorption to a solid surface is called “physisorption”. It takes place if the interaction is mainly due to the ubiquitous van der Waals interaction and typical binding energies are lower than 50kJ/mol. On the contrary, if gas particles that strike the surface bind to it through the formation of a surface chemical bond “chemisorption” occurs and typical binding energies are higher than 50 kJ/mol and comparable to a fraction of the substrate sublimation energy. Moreover we should remark that chemisorption is an activated process, i.e. the formation of a chemisorptive bond requires the overcoming of an activation barrier. 1.2 Adsorption and desorption kinetics 1.2.1 Adsorption isotherms Theories from which arise studies about adsorption and desorption phenomena are essentially based on the following principles:  Adsorption is a localized phenomenon, i.e. absorbed particles are motionless  The substrate surface is saturated when all its adsorption sites are occupied, so a monolayer is formed : Θ = 1ML, with surfads NN , (1.1) where Nads is the adsorption particles number , while Nsurf represents the number of adsorption sites on surface.  There is not interaction between adsorbed particles. Adsorption is usually described through isotherms, that is, the amount of adsorbate on the adsorbent as a function of its pressure at constant temperature. The most important adsorption isotherm in the analysis of adsorption/desorption phenomena is the Langmuir isotherm, described through the following set of equations:       n ndes n nad Br pAr   1 , (1.2) with An and Bn constants, n=1,2 and rad/des the adsorption/desorption rate. From the dynamic equilibrium condition, desad rr  , it follows that: 5     n n n n n pb pb 1 1 1  . (1.3) For n=1 it is possible to observe an adsorption/desorption first order which corresponds to a sort of condensation process of adsorbed molecules on the surface, while for n=2 there is a second order process, which corresponds to a dissociative adsorption and to a recombining desorption for diatomic molecules. Moreover molecules dissociation can be reduced decreasing surface temperature. Other common desorption isotherms are the Freundlich (4) and Brunauer, Emmett e Teller isotherms (BET)  p n  , with 0.2<β<1.0 (1.4)   0maxmax0 11 p p C C Cpp p      , (1.5) where p0 = vapour pressure of purely liquid phase at fixed temperature C = system specific constant γ = adsorption molality,  LAads NmN  (1.6) γmax = the maximum molality that can be achieved whit a monoatomic layer mA = mass of the adsorbed particle. The Bet isotherm extends the assumptions of Langmuir isotherm to multiple layers. It is hypothesized that only the first monoatomic layer is bonded to substrate surface and that, consequently, all the adsorbed layers are characterized by the same bonds that correspond to adsorbed molecules in liquid phase. This model describes chains of not interacting adsorbed molecules that grow perpendicularly to surface, so it is assumed that each molecule of the chain has coordination number of 2. For multiple coverages results achieved from BET isotherm are very different from experimental isotherms [2]. 6 1.3 Polanyi-Wigner equation Adsorption of gaseous molecules on a solid surface, with pressure and temperature fixed, is governed by the equality of the chemical potential of the adsorbed layers and of the gas μad(N) = μgas(P,T), where N is the number of molecules adsorbed on surface, characterized by a total number of adsorption sites of N0. The chemical potential of the adsorbed species is usually calculated through different techniques (ex. density functional method), while μgas(P,T) can be obtained by thermal dynamics consideration. For a gas the Gibbs free Energy is defined as G= H- TS = U + PV-TS, (1.7) where H ,S and U are respectively the enthalpy, the entropy and the energy of the system. For isothermal adsorption at a temperature Tad dG= VdP, so   G G P P VdPdG 0 0 , (1.8) from which  P P VdPGG 0 0 . (1.9) The chemical potential is defined as the molar Gibbs free energy μ=dG/dn, so 0 0 P P V dP n     . (1.10) For an ideal gas 0 0 ln P P RTad  , (1.11) where μ0 is the chemical potential at the reference pressure P0. If the gas is not ideal is necessary to calculate the integral in equation (1.10) using the equation of the state. For example, for the van der Waals interaction, V can be expressed as a series of P: 7 ) 1 ( cPb P nRTV  , (1.12) where the virial coefficients b and c are temperature dependent and the values can be found in literature. The desorption rate is usually expressed through a law of n th (with n = 0,1,2): n ndes k dt d r    (1.13) If the rate constant kn is described by Arrhenius equation           RT E k PW des nn exp , (1.14) with νn = desorption frequency, equation (1.13) becomes: n PW des ndes RT E dt d r             exp , (1.15) that define the activation Energy of desorption PW desE and it is important in the interpretation of the experimental spectra. It is useful to observe the differences between the three kinetic orders: i)Zero kinetic order 0 (n=0)  Desorption rate is not dependent on coverage.  Desorption exponentially increases with T.  When dose increases the desorption peak moves to higher temperatures (fig.1.2). Fig. 1.2. Representation of a zero-order kinetic 8 ii) First kinetic order (n=1)  Desorption rate is directly proportional to coverage.  When coverage increases the temperature at which the maximum of the peak occurs does not vary (fig.1.3).  The peak is asymmetrical. Fig. 1.3. First-order kinetic iii) Second kinetic order (n=2)  Desorption rate varies with the square of the coverage.  The temperature at which maximum of the peak occurs increases with decreasing of the coverage (fig.1.4).  The peak is symmetrical. Fig. 1.4. Second-order kinetic 9 Zero-order kinetics are often indicative of desorption from a multilayer where the rate of desorption is independent on surface coverage; first-order kinetics may be indicative of the presence of a single surface species; second-order kinetics are an indication of adsorbate atom recombination process leading to the production of a diatomic molecules. A fundamental condition to determinate a thorough set of data is that the observed desorption signal is proportional to desorption rate; each step of the desorption process has to take place more slowly than any secondary reaction involved (rate-limiting). In equation (1.15) it is possible to note that the activation parameters depend generally from the coverage, but often it is possible a dependence from temperature, in particular a dependence from the heating rate β, an experimental parameter. So it is reasonable to think that thermal desorption technique gives information about nature of adsorbed molecules in conditions very distant from equilibrium and at temperatures lower than desorption temperature; as a consequence the Polany-Wigner equation can result insufficient for analysis and it is possible to couple with it equations based on simulation of desorption spectra with complex statistic models to describe the interactions of adsorbates [2]. 1.3.1 Material balance equation for Thermal Desorption in a vacuum system The basic equations for the measurement of thermal desorption spectra are given below [1]. The desorption rate (Rd) of a species from a surface should be a function of the surface concentration N and of the temperature T of the species. The Arrhenius form is  kTEnn d deNR dt dN   )( 0 , (1.16) where )( 0 n is the pre-exponential factor, n the desorption order (usually n=0,1,2) and Ed the activation energy for desorption. It is often assumed as a first approximation that )( 0 n and Ed are constant, but it has been shown that in many cases these kinetic parameters vary with coverage N. If the pumping speed of the system (s) is constant, if the pressure rise P above the base pressure P0 is used and if no adsorption/desorption processes occur on extraneous surface, the Redhead equation is [6]   V Ps dt dN A V kT dt Pd          (1.17) 10 = (rate of the gas evolution) –(incremental pumping rate above steady state background rate). Thus, AkT Ps dt Pd AkT V Rd     )( , (1.18) which may be rewritten as  P dt Pd V AkT Rd     )( , (1.19) where η = V/s is the characteristic pumping time of the system. Defining a characteristic time δt for the desorption of a binding state, two limits exist:  for η >> δt the Eq.1.19 becomes dt Pd AkT V Rd )(  ; (1.20)  for η << δt  P AkT V Rd   . (1.21) For most situations involving vacuum system with fast pumping speed (η0.25s) and δt 2s, Eq. (1.21) is applied conveniently and the pressure rise P is a direct measure of the desorption rate Rd. For intermediate cases it is convenient to use both terms in Eq. (1.19). In a glass or metal ultrahigh-vacuum system it is possible to measure η by rapidly opening or closing the leak valve for the gas admission or by producing a pulse of gas by rapid desorption from a filament and, subsequently, following the decay of pressure with time. It is often found that η is not constant. This problem may be due to wall effect or to re-emission of gas from ion pumps or other element within the system. Redhead [7] proposed a method to determinate that wall effects are absent in adsorption/desorption experiments under flow conditions. The pumping speed of a gas under molecular flow conditions (with no wall effects) is directly proportional to the molecular mean velocity and, for a Boltzmann distribution, it is therefore proportional to (mT) -1/2 , where m is the molecular mass. 11 1.4 Theories of Thermal desorption 1.4.1 The Mobile Precursor Model in Adsorption and Desorption Several studies about chemisorption on surfaces have shown that the sticking coefficient remains nearly constant (and often near unity) over a wide coverage range. This observation has led to the postulate that in chemisorption is present a precursor state , that may sample both filled and empty adsorption sites as it migrate, until finally becoming chemisorbed [1]. King [3] was the first to propose the passage through a mobile precursor state also in thermal desorption and he computed the influence that this process might have on the shape of thermal desorption spectra. Gorte and Schmidt [4] have formulated a desorption kinetic model involving transition through a precursor state, illustrated below for first-order desorption kinetics. For an adsorbed molecule A(s), the elementary reaction describing desorption process is (1.22) where the k’s represent first-order rate constants for the elementary steps. If the precursor state A * is in equilibrium with A(s) at coverage θs and it is at a low steady- state concentration during desorption, is it possible to write   01 *** *  ASAasdA kkkdtd  (1.23) and   SaSdAS kkkkkdtd   1*** * . (1.24) For k * >>ka the first-order desorption kinetics is obtained sdS kdtd   ; (1.25) while for k * <