2015 International Conference on Accelerated Carbonation for Environmental and Material Engineering (ACEME)

CO2 Chemisorption and Structural Analyses of the Na2(Zr1-xAlx)O3-x/2 Solid Solution

Authors

Alcántar-Vázquez, B. - Presenter, Instituto de Investigaciones en Materiales, UNAM
Gómez-García, J. F., Facultad de Química, UNAM
Lima, E., Instituto de Investigaciones en Materiales, UNAM
Pfeiffer, H., Instituto de Investigaciones en Materiales, UNAM

Different alkaline ceramics, mainly lithium or sodium, show excellent CO2 capture properties.1-3 Among them, zirconates have been reported as good candidates as CO2 solid sorbents. In 2004 it was reported that Na2ZrO3 is able to absorb CO2 at 600 °C. Since then, several works have reported that Na2ZrO3 presents much better characteristics as CO2 captor in comparison with Li2ZrO3.4-6 It has been explained because Na2ZrO3 has a lamellar structure, where sodium atoms are located among the (ZrO3)2 layers, which favors sodium diffusion porcesses.4               

On the other hand, different structural and/or chemical modifications have been carried out in order to enhance the CO2 chemisorption of this kind of ceramics. For example, different solid solutions such as Li2xNaxZrO3, Li3.7Al0.1SiO4, Li3.7Fe0.1SiO4 and Li4xNaxSiO4 have been evaluated as possible CO2 captors.5,7-9 In general, all these solid solutions have shown an improvement on different properties of the CO2 chemisorption reaction, in comparison to their respective pure alkaline ceramics. The improvements observed on these solid solutions have been attributed to the point defects formation into the lattice or to the secondary phase production.

            Therefore, the aim of the present work was to analyze both structural and microstructural characteristics of Na2(Zr1xAlx)O3-x/2 solid solution as a function of the CO2 chemisorption capacities.

To determine the influence of the aluminum content in the sodium zirconate during the CO2 chemisorption process, specific compositions in the Na2(Zr1xAlx)O3-x/2 solid solution were synthesized via a solid-state reaction. Samples were characterized using X-ray diffraction (D8 Bruker diffractometer), N2 adsorption-desorption (Minisorp II equipment from BEL Japan) and 27Al solid-state nuclear magnetic resonance (Bruker Avance II spectrometer). Then, samples were tested as CO2 captors using dynamic and isothermal analyses with Q500HR equipment, from TA Instruments. The samples were dynamically heated from room temperature to 800 at 5 °C/min. These analyses were carried out under a saturated CO2 atmosphere (60 mL/min). For the isothermal analysis, the samples were initially heated to 850 °C using a N2 flow. This initial thermal step was performed to eliminate any previous sample carbonation. Then, each sample was cooled down to its respective isothermal temperature (between 300 and 700 °C) to perform independent CO2 chemisorption processes. As the sample reached the corresponding temperature, the gas flow was switched from N2 to CO2.

            Additionally, ionic conduction experiments were performed in different samples to determine the effect of these phases during the CO2 chemisorption process. For these experiments, fine grain powders of the samples were pressed in the form of pellets of about 1 cm in diameter and 0.1cm in thickness. Then, each pellet was heated at the sintering temperature of each compound, and the top and bottom pellet surfaces were coated with gold (as oxygen-ion blocking electrode), using a sputtering technique. The measurements were performed in a quartz cell coupled to a vacuum system (800-700 mTorr) and heated between 400 and 800 °C. Both sample sets were analyzed using the 2-point DC technique, and platinum wires as electrodes.

XRD results show that Na2ZrO3 and Na2(Zr1−xAlx)O3-x/2 solid solution corresponds to the monoclinic Na2ZrO3 crystalline phase (35-0770 JCPDS diffraction file). After the crystalline verification of the samples, some microstructural properties were determined by N2 adsorption-desorption. The samples showed N2 adsorption-desorption type II isotherms, with very narrow H3-type hysteresis loop, according to the IUPAC classification. This behavior corresponds to non-porous materials frequently obtained by solid state synthesis. Then, the surface areas were measured using the BET method, obtaining very similar values, ≤ 1 m2/g, in all cases. Besides, the 27Al solid-state NMR results showed that aluminum atoms are located at the zirconium or sodium crystalline positions in the Na2ZrO3 structure (tetrahedral or octahedral positions, respectively). Thus, the aluminum dissolution is compensated by different structural defects. The CO2 capture evaluation shows that the aluminum presence into the Na2ZrO3 structure improves the CO2 chemisorption within certain aluminum content and under specific thermal conditions. Samples of the Na2(Zr1xAlx)O3-x/2 solid solution were able to chemisorb CO2 in a wide temperature range (200−700 °C), exhibiting higher CO2 chemisorptions than Na2ZrO3. These results were corroborated kinetically. In fact, isothermal experiments shows that the Na2ZrO3 is the sample that chemisorbed CO2 at a slower rate in comparison with the compounds of the Na2(Zr1xAlx)O3-x/2 solid solution. Isotherms were fit to double or triple exponential models; where the observed reaction steps are: (1) CO2 chemisorption over the surface of the Na2(Zr1xAlx)O3-x/2 particles, (2) CO2 chemisorption kinetically controlled by diffusion processes, and (3) CO2 desorption process. The last process was detected only between 200 and 400 °C. The kinetic constant values indicated that the CO2 chemisorption kinetically controlled by diffusion processes is the rate-limiting step for the whole process. Additionally, ΔH values were calculated using the Eyring’s model and they tended to increase when the aluminum was increased. This result indicated a higher thermal dependence of the CO2 chemisorption as a function of the aluminum content. Additionally, the cyclic experiments indicate that Na2(Zr1xAlx)O3-x/2 solid solution samples exhibited high and stable CO2 capture behaviors.10

Finally, the sodium ionic conductivity, of different phases, was analyzed to complement the CO2 chemisorption mechanism in these materials. The analyzed phases were; Na2ZrO3 and Na2(Zr0.9Al0.1)O2.95 as initial chemisorbents, as well as Na2CO3 and NaAlO2 as the different sodium phases produced in the external shell. The ionic conductivity and activation energy of the Na2(Zr0.9Al0.1)O2.95 are smaller than those in Na2ZrO3. This result was is in good agreement with the initial ΔGf thermodynamic theory, establishing that Na-O bond must become weaker in the aluminum containing compounds. However, if the ionic conductivity activation energy of NaAlO2 and Na2CO3 (sodium phases present at the external shell) are compared, the activation energy in the NaAlO2 case is higher than that in Na2CO3. Thus, the ionic conductivity processes in the external shell are limited by the NaAlO2 presence.

Therefore, the results presented here confirm that aluminum atoms are incorporated into the Na2ZrO3 structure, occupying zirconium and sodium atom sites. The samples of the Na2(Zr1xAlx)O3-x/2 solid solution, with aluminum atoms localized at octahedral sites, were able to chemisorb CO2 in a wide temperature range (200−700 °C), exhibiting higher CO2 chemisorptions than Na2ZrO3. The CO2 chemisorption differences were attributed to several factors such as the presence or absence of different structural vacancies and the presence of different secondary phases in the carbonated external shell. Finally, NaAlO2 formation must be mainly responsible for the drop in the CO2 chemisorption that is experimentally observed.

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