IX Simposio Colombiano de Catálisis (SiCCat)⁺

ETHYL ACETATE OXIDATION OVER MnO_x-CoO_x. RELATIONSHIP BETWEEN OXYGEN AND CATALYTIC ACTIVITY

OXIDACIÓN DEL ACETATO DE ETILO SOBRE MnO_x-CoO_x. RELACIÓN ENTRE OXÍGENO Y ACTIVIDAD CATALÍTICA

OXIDAÇÃO DO ACETATO DE ETILO SOBRE MnO_x-CoO_x. RELAÇÃO ENTRE OXIGÊNIO E ATIVIDADE CATALÍTICA

María-Haidy Castaño-Robayo¹, Rafael Molina-Gallego¹ and Sonia Moreno-Guáqueta*¹

¹Estado Sólido y Catálisis Ambiental (ESCA), Departamento de Química, Facultad de Ciencias, Universidad Nacional de Colombia, Bogotá, Cundinamarca, Colombia

e-mail: smorenog@unal.edu.co

How to cite: Castaño-Robayo, M. H., Molina-Gallego, R. & Moreno-Guáqueta, S. (2015). Ethyl acetate oxidation over MnO_x-CoO_x. Relationship between oxygen and catalytic activit. CT&F - Ciencia, Tecnología y Futuro, 6(2), 45-56.

*To whom correspondence should be addressed

(Received: Sep. 28, 2015; Accepted: Dec. 02, 2015)

ABSTRACT

Catalytic oxidation is an alternative for the transformation of volatile organic compounds. Mn and Co catalysts are the most active in oxidation reactions because of their redox properties and oxygen mobility. Co-precipitation is one of the methods most used to prepare metal oxides. In this regard and in order to understand the relationship between oxygen species and the activity of the catalysts, in this work mixed oxides of Co-Mn-Mg-Al were prepared by the co-precipitation method. The catalysts were characterized by XRD, surface area, temperature-programmed desorption of oxygen, oxygen storage capacity, ¹⁸O/¹⁶O isotopic exchange; and the catalytic activity was evaluated in the oxidation of ethyl acetate. The results indicate that manganese-containing oxides have surface adsorbed oxygen and a greater amount of oxygen susceptible to redox cycles while oxides containing cobalt show high oxygen mobility. In the oxidation of ethyl acetate, the most labile oxygens undergo redox cycles and surface adsorbed oxygens are the species involved.

Keywords: Hydrotalcite, Mixed oxide, Mobility, Oxygen storage capacity.

RESUMEN

La oxidación catalítica es una alternativa promisoria para la transformación de contaminantes atmosféricos como los compuestos orgánicos volátiles. Los catalizadores basados en óxidos de Mn y Co se encuentran dentro de los más activos en las reacciones de oxidación debido a sus propiedades redox y su movilidad de oxígeno. La co-precipitación es uno de los métodos más empleados para preparar óxidos metálicos por las propiedades únicas que presentan los sólidos finales. En tal sentido y con el fin de comprender la relación existente entre las especies de oxígeno y la actividad de los catalizadores, en éste trabajo se prepararon óxidos mixtos de Mn-Co-Mg-Al mediante la metodología de coprecipitación. Los catalizadores se caracterizaron por difracción de rayos X, área superficial, desorción de oxígeno a temperatura programada, capacidad de almacenamiento de oxígeno e intercambio isotópico ¹⁸O/¹⁶O; adicionalmente, se evaluó la actividad catalítica en la oxidación del acetato de etilo. Los resultados indican que los óxidos que contienen manganeso presentan especies de oxígeno adsorbidas superficialmente y una mayor cantidad de oxígenos susceptibles de sufrir ciclos redox mientras que los óxidos que contienen cobalto demuestran la presencia de oxígenos con mejor movilidad. En la oxidación del acetato de etilo, los oxígenos más disponibles de conducir ciclos redox y los oxígenos adsorbidos en la superficie resultan ser el factor determinante.

Palabras clave: Hidrotalcita, Óxido mixto, Movilidad, Capacidad de almacenamiento de oxígeno.

RESUMO

A oxidação catalítica é uma alternativa promissória para a transformação de contaminantes atmosféricos como os compostos orgânicos voláteis. Os catalizadores baseados em óxidos de Mn e Co se encontram dentro dos mais ativos no que tange as reações de oxidação por conta de suas propriedades redox e sua mobilidade de oxigênio. A co-precipitação é um dos métodos mais utilizados para preparar óxidos metálicos graças às propriedades únicas exibidas pelos sólidos finais. Nesse sentido e no intuito de compreender a relação existente entre as espécies de oxigênio e atividade dos catalizadores, neste trabalho preparamos óxidos mistos de Mn-Co-Mg-Al mediante a metodologia de co-precipitação. Os catalizadores se caracterizaram pela difração de raios X, área superficial, dessorção de oxigênio a temperatura programa, capacidade de armazenamento de oxigênio e intercâmbio isotópico ¹⁸O/¹⁶O; além disso, a atividade catalítica na oxidação do acetato de etilo também foi avaliada. Os resultados indicam que os óxidos que contém manganês apresentam espécies de oxigênio adsorvidas superficialmente e uma maior quantidade de oxigênios suscetíveis de sofrer ciclos redox enquanto os óxidos que contêm cobalto apresentam oxigênios com melhor mobilidade. Na oxidação do acetato de etilo, os oxigênios mais disponíveis para a condução de ciclos redox e os oxigênios adsorvidos na superfície são o fator determinante.

1. INTRODUCTION

It has been reported that the adsorbed oxygen species on the surface defects together with the lattice oxygens with high mobility are responsible for the oxidation reactions on metallic oxides (Moro-oka, Ueda & Lee, 2003). In the oxidation of propene on CoCe oxides a direct relation between the redox properties and the catalytic behavior was found due to the high oxygen mobility present in these solids. On a Ce single oxide the adsorbed oxygen species on surface vacancies are involved (Liotta et al., 2008). Likewise, in the oxidation of propane on a MnNi catalyst a high activity is observed due to the presence of surface oxygen species (denominated α) while in the oxidation of ethanol a MnFe catalyst exhibits the best catalytic by the participation of lattice oxygens (denominated β), which play an important role in the process (Morales, Barbero & Cadús, 2007).

Regarding mixed Mn and Co oxides derived from hydrotalcite type precursors, there is scarce information about the oxygen species involved in the oxidation of Volatile Organic Compounds (VOCs). This work focuses on studying the species of oxygens present in these materials employing the techniques of temperature-programmed desorption of oxygen (O₂-TPD), Oxygen Storage Capacity (OSC) and ¹⁸O/¹⁶O isotopic exchange in order to establish a correlation between these species and the catalytic behavior.

2. THEORETICAL FRAME

VOCs can be defined as “those organic compounds which at a temperature of 20°C present a vapor pressure of 0.01 kPa or superior or a volatility equivalent to the particular conditions of use” (Garetto, Legorburu & Montes, 2008).

The abatement of VOCs is of great importance since their emission is hazardous to the environment and human health. The VOCs are involved in the formation of “photo-chemical smog”, some are toxic, carcinogenic or teratogenic and many of them are connected to the greenhouse effect (Koppmann, 2010).

Thermal and catalytic oxidation are the most efficient methods to eliminate VOCs emission ( ̴ 99%). However, thermal oxidation requires a high operating temperature consuming significant amounts of energy and producing high levels of nitrogen oxides (NOx). Catalytic oxidation reduces the oxidation temperatures and, in consequence, generates a smaller quantity of NOx (Khan & Ghoshal, 2000).

Metallic oxides are among the materials most used in the catalytic oxidation due to their great electronic mobility and high resistance to deactivation by their high surface areas (Garetto et al., 2008; Spivey, 1987). A common characteristic of metallic oxides in the oxidation of VOCs is the presence of multiple states of oxidation, which enables the formation of redox cycles where the metal is reduced by the VOC and re-oxidized by the oxygen of the current.

Manganese and cobalt oxides are promising catalysts in oxidation reactions since they show a high capacity to form oxides in different states of oxidation, elevated capacity of oxygen storage and a optimum strength of the M-O bond (Fierro, 2006; Liotta et al., 2013).

Layered Double Hydroxides (LDH) also known as anionic clay or Hydrotalcite Type (HT) represent a kind of synthetic laminar materials whose general formula could be expressed as , where M²⁺ and M³⁺ represent divalent and trivalent cations respectively, A^n- an anion and x which must be found in the interval between 0.2 and 0.33 to preserve the structure; if x is out of this range, hydroxides and other compounds can be formed (Kovanda & Jirátová, 2011; Xu et al., 2011).

The hydrotalcite structure is related to that of brucite Mg(OH)₂ where the Mg²⁺ is octahedrally coordinated with six hydroxile groups and the octahedrons generated share their sides to form bi-dimensional layers, which stay joined by Van der Waals forces. The replacement of some cations for example Mg²⁺ for Al³⁺, creates positive charges that are compensated for by the presence of anions in the interlayer spacing forming the hydrotalcite structure.

The Mn²⁺ and Co²⁺ cations are capable of completely or partially replacing the Mg²⁺ ions within the laminar structure forming LDH materials of different compositions. The thermal decomposition of the hydrotalcites allows us to obtain mixed oxide with important industrial applications involving the use of catalysts (Xu et al., 2011).

3. EXPERIMENTAL

Catalysts Synthesis

Solutions of the respective nitrates were used maintaining the ratios M²⁺/M³⁺ = 3, M²⁺/Mg²⁺ = 1 (where M = Mn²⁺, Co²⁺ or Mn²⁺+Co²⁺). For the Mn and Co oxide the ratio Co²⁺/Mn²⁺ = 0.5 was preserved. The Mg²⁺, Al³⁺, Mn²⁺ and/or Co²⁺ nitrates were mixed and added dropwise to a solution 0.2 M of K₂CO₃ with constant stirring, maintaining pH level between 9.5 and 10.5 (addition of a solution of NaOH 1 M). The precipitate obtained was aged for 18 h without stirring. Subsequently, all the solids obtained were washed and dried at 60°C in air for 18 h to obtain the respective hydrotalcite type precursors denominated HTMn1.0, HTCo1.0 and HTCoMn0.5.

The hydrotalcites were calcined at 500°C for 16 h to generate the respective mixed oxides denominated CPMn1.0, CPCo1.0 and CPCoMn0.5 (were CP indicate co-precipitation).

Characterization

X Ray Diffraction

N₂ Adsorption

Micromeritics^® ASAP 2020 equipment was used. The samples were degassed at 350°C for 4 hours and then the N₂ adsorption-desorption isotherms were carried out at -196°C.

Temperature-Programmed Desorption of Oxygen (O₂-TPD)

The mixed oxides (0.100 g) were degassed at 400°C for 1 h in the presence of He. The adsorption of O₂ (9.99% O₂ in He) was carried out at 400°C and at room temperature under the same atmosphere 1 h for each temperature. A flux of 50 mL·min⁻¹ of He was used to remove the excess O₂ and finally desorption of the O₂ was carried out by increasing the temperature on a heating ramp of 10ºC·min^-1 to 900°C. Origin^®Pro 8.5 software was used to quantify the areas associated with desorption of O₂.

Oxygen Storage Capacity (OSC)

The analyses were conducted using equipment built by the ESCA group employing the H₂/O₂ pulse injection technique (Christou et al., 2012). Prior to carrying out the measurements, samples (0.015 g in 0.100 g of SiC) were pre-oxidized under an air flow of 10 mL·min^-1 (21% O₂) at 400°C for 40 min and with a subsequent argon step until the ¹⁶O₂ signal was not detected. Later, the samples were cooled to 200°C under an argon flow (10 mL·min^-1) and alternating pulses of H₂-O₂ of 50 µL each were carried out completing two cycles. In order to know the quantity of oxygen most available to the solids in a range of temperatures, the same procedure was applied at temperatures close to 275, 345 and 400°C. The concentrations of the H₂, O₂, H₂O, Ar and He gases were monitored by mass spectrometry (Omnistar mass spectrometer) following the signals m/z = 2, 32, 18, 40 and 4, respectively.

The OSC was calculated based on the quantity of oxygen consumed during the re-oxidation stage after carrying out the H₂ pulses, and these are expressed in terms of µmol O₂·g^-1 of catalyst. Origin^®Pro 8.5 software was used to quantify the areas of each of the pulses associated with the O₂ signal.

¹⁸O/¹⁶O Isotopic Exchange

The samples (0.030 g with 0.100 g of SiC) were treated under an air flow (10 mL·min^-1) at 400°C for 1 h. Then, cooling was permitted to 200°C under an argon flux. Pulses of 20 µmL ¹⁸O₂ were carried out on the samples at 200, 260, 330 and 400°C in presence of an argon flow (10 mL·min^-1). Gas composition was monitored by mass spectrometry (Omnistar mass spectrometer) following the signals m/z = 36, 34 and 32 corresponding to ¹⁸O₂, ¹⁸O ¹⁶O and ¹⁶O₂, respectively. Origin^®Pro 8.5 software was used to quantify the areas below the signals associated with the concentration of ¹⁸O₂, ¹⁸O ¹⁶O and ¹⁶O₂.

A fixed bed reactor at atmospheric pressure in the temperature range of 400 to 150°C was used in the catalytic evaluation. Samples (0.200 g sieved < 250 μm) were pretreated in an air flux (21% O₂) at 400°C for 1 hour. The conversion curves were obtained by cooling at 1.5°C·min^-1 from 400 to 150°C maintaining a total flow of 280 mL·min^-1 of air with 1000 ppm of ethyl acetate. Reaction products and reactives were analyzed in line with a Shimadzu GC-17A gas chromatograph, and CO₂ production, by a Bacharach Model 3150 CO₂ analyzer equipped with an IR detector.

CO₂ conversion was calculated following the stoichiometry of the reaction and employing the following expression:

4. RESULTS

Precursors of Mixed Oxides

The diffraction patterns of the manganese and cobalt hydrotalcites, HTMn1.0, HTCo1.0 and HTCoMn0.5 are presented in Figure 1 where they are compared to the diffractogram typical of a Mg-Al hydrotalcite (HTMgAl). The presence of intense signals at 11.3, 22.6 and 34.4 °2θ in the XRD patterns indicates the formation of a well crystallized laminar structure with 3R symmetry in all cases (Tsyganok & Sayari, 2006).

For HTCo1.0 the only phase identified corresponds to the hydrotalcite phase (JCPDS 70-2151) without observing any other phases associated to cobalt, which suggests its homogeneous incorporation in the hydrotalcite structure.

HTMn1.0 reveals the signals of the hydrotalcite of reference (HTMgAl) and signals attributed to hausmanite phase Mn₃O₄ (JCPDS 24-0734), rhodochrosite MnCO₃ (JCPDS 44-1472) and possible formation of Mn(OH)₂ phase (JCPDS 73-1604. Formation of Mn₃O₄ occurs for the oxidation Mn²⁺ to Mn³⁺ in the synthesis conditions. Presence of Mn(OH)₂ and MnCO₃ phases has been reported in Mn hydrotalcites with Mn_xMg_3-xAlO formula (x varies in the range of 0 to 3), suggesting that at least 37.5% of the Mg and Al ions can be isomorphically substituted by the Mn in the hydrotalcite (Lamonier et al., 2007; Li et al., 2010; Velu et al., 1999).

Mixed Oxides

It has been widely reported that the thermal decomposition of Mg-Al hydrotalcites begins with the loss of water molecules in the interlayers at 150-200°C, followed by the collapse of the hydroxile layers in the temperature range of 300-400°C and, finally, the complete loss of the laminar structure over 500°C (Tsai et al., 2011). Figure 2 shows the diffraction patterns of the manganese, cobalt and manganese-cobalt oxides generated from the thermal decomposition of the corresponding hydrotalcite at 500°C for 16 h. The profiles do not reveal signals associated with the hydrotalcite phase, confirming the total destruction of the laminar structure and the formation of the corresponding mixed oxides.

All the mixed oxides reveal signals of the periclase phase (MgO). Additionally, CPMn1.0 shows peaks attributed to the presence of manganese spinels, Mn₃O₄ (JCPDS 70-2151), MnAl₂O₄ (JCPDS 029-0880) and Mg₂MnO₄ (JCPDS 19-0773).

In the case of oxide CPCo1.0, the phases of type CoAl₂O₄, Co₂AlO₄ and Co₃O₄ (JCPDS 044-0160; JCPDS 030-0814; JCPDS 042-1467 respectively) could be present. Due to the amplitude of the signals and the complexity of the peaks in the oxide mixed diffratograms it is impo-ssible to assign the signals to a specific phase.

CPCoMn0.5 exhibits the same signals as the manganese and cobalt oxides with the possible formation of solid solutions of the Mn_3-xCo_xO₄ type (x =0 to 3) (Bordeneuve et al., 2009; Jang, Wang & Chiang, 1998). Taking into account that for the synthesis of CPCoMn0.5 a ratio Co/Mn = 0.5 was used where the Mn is in a greater proportion, the possible formation of the hausmanite phase (Mn₃O₄) is to be expected with the isomorphic substitution of Mn for Co within the structure to form a solid solution of the Mn_3-xCo_xO₄, type, which would explain the similarity of the diffraction profiles of CPCoMn0.5 and CPMn1.0.

The N₂ adsorption-desorption isotherms of the mixed oxides are shown in Figure 3a. All oxides reveal type II isotherms characteristic of macro-porous materials. The presence of an H1 hysteresis loop evidences the presence of pores with uniform sizes and forms in the materials. The specific area is attributed to the formation of pores resulting from the destruction of the laminar spaces following the calcination (loss of water and carbonates)(Aguilera et al., 2011). The area values determined by means of the BET model for CPMn1.0, CPCo1.0 and CPCoMn0.5 corresponding to 186, 154 and 162 m²·g^-1, respectively. The lower value in area of solids CPCo1.0 and CPCoMn0.5 can be attributed to the formation of the spinels with the aluminum, as shown by the XRD analysis, which reduce the textural properties (Mo et al., 2003; Muñoz, Moreno & Molina, 2012).

The distribution of the pore size of the oxides is presented in Figure 3b. A wide range of pore sizes from 5 to 90 nm approximately is observed in all the oxides, confirming the meso and macro-porous character of these materials.

O_2(ad)→ O_(ad)→ O^-_(ad) → O^2-_(bulk), where the desorption signals at temperatures lower than 400°C ascribed to oxygen species (α) like O^2- and O^- which are weakly linked at the surface, whereas the signals that appear at temperatures greater than 400°C are assigned to lattice oxygens (β) which are found in diverse chemical environments (Liotta et al., 2008; Xue et al., 2007). The O₂-TPD profiles of the mixed oxides CPMn1.0, CPCo1.0, and CPCoMn0.5 are shown in Figure 4.

CPMn1.0 shows a desorption peak centered at 250°C (species α) showing that this oxide has an important concentration of surface oxygen species. The signal at 244°C has been attributed to the desorption of oxygen species of the Mn₃O₄ phase (Arnone et al., 1998), a temperature very close to that found in CPMn1.0 indicating the presence of the hausmanite in this oxide as was evidenced by XRD. Also, this solid presents different desorption signals at T > 400°C which correspond to lattice oxygens (species β) with different chemical environments or different oxygen mobility (Santos et al., 2009).

In the profile of CPCo1.0 different signals are observed in the temperature range of 400 - 900°C, which can be assigned to bulk oxygen species with different bond strength or oxygen mobility. The signal at 700°C can be attributed to the thermal decomposition of the Co₃O₄ to CoO (Liotta et al., 2008).

Mixed oxide CPCoMn0.5, exhibits signals at temperatures greater than 400°C very similar to those found in CPMn1.0 and CPCo1.0. The absence in this oxide of the signal at ~250°C characteristic of the Mn₃O₄ phase can indicate the partial substitution of the Mn by Co in the structure of the hausmanite. Likewise, the great intensity of the peak to 640°C in CPCoMn0.5 suggests that the oxygen adsorbed species fill the internal vacancies created by the substitution of Co by Mn (Merino et al., 2005). This results evidence the formation of a solid solution of Co-Mn, which leads to a cooperative effect between the phases, increasing oxygen mobility in CPCoMn0.5 as compared to CPMn1.0 oxide.

It is well known that the catalyst used in oxidation must have a large number of sites capable of linking with the oxygen molecules and also, that have a great ability to donate and accept electrons (Oyama, 1996).

Regarding mixed oxides the redox process can be described in terms of the following general mechanism:

The catalyst (Cat-O) is reduced by the substrate (reducer), which is subsequently re-oxidized by an oxidizer (Ox-O) to its initial state. The net result is the transference of oxygen to one species or another, which in the specific case of VOCs, is carried out by the oxidation of the organic compound and the reduction of the surface of the oxide due to the loss of surface oxide ions and the subsequent re-oxidation of the catalyst (Fierro, 2006).

For studying the most labile or reactive oxygen species that can participate in oxidation reactions and determine the redox ability of the Mn and mixed oxides, which simulates the transfer of electrons in the oxidation mechanism of VOCs, we used the OSC technique.

Figure 5 shows the OSC of the mixed oxides under dynamic conditions at different temperatures (200-400°C). The OSC increases with the rise of the temperature since at low temperatures (below 300°C) the surface and near-surface oxygen makes major contribution to OSC and at higher temperatures (above 300°C) bulk oxygen migration plays an important role to determine the OSC performance (Wang et al., 2011; Zhao, Shen & Wang, 2007).

Figure 5 shows that the manganese-containing oxides exhibit OSC values greater than CPCo1.0 being CPCoMn0.5 the one that presents the most important values. This result is attributed mainly to the incorporation of Co in the structure of the manganese oxide (CPMn1.0) that can increase the migration of the bulk oxygen generating vacancies which form very weak bonds with the oxygen species (Wang et al., 2011).

The oxygen mobility of the oxides is an important factor in oxidation reactions given that if the oxygen species present sufficient mobility, the lattice oxygens can become involved in the catalytic process (Spivey, 1987; Yamazoe & Teraoka, 1990). The isotopic exchange technique provides information regarding oxygen mobility in terms of the exchange capacity of the oxygen species present in the materials. There are three routes by which the ¹⁸O/¹⁶O exchange can be undertaken (Nováková, 1971; Royer, Duprez & Kaliaguine, 2005):

1. Homogeneous exchange: This reaction does not require the participation of the oxygen atoms of the solid and the concentrations of ¹⁶O and ¹⁸O remain constant during the test:



2. Simple heterogeneous exchange: Involves an oxygen atom of the oxide and an oxygen atom of the gaseous phase.



]]> Multiple heterogeneous exchange: This mechanism involves the participation of two of the atoms of the solid in each step.

The variation of the concentrations of ¹⁶O₂, ¹⁶O¹⁸O and ¹⁸O₂ in the three oxides during the tests shows that the predominant exchange in these materials corresponds to the heterogeneous exchange (Figure 6).

A way of comparing exchange capacity among the materials and therefore oxygen mobility is in terms of the concentration of ¹⁶O₂, where the oxide which presents the greatest concentration of ¹⁶O₂ will be the solid with the greatest oxygen mobility. CPCo1.0 exhibits the highest concentrations of ¹⁶O₂ and therefore the greatest oxygen mobility at all oxides in the temperatures tested.

Ethyl acetate is a compound found in the paint, cosmetics, industrial dyes and is considered one of the most difficult molecules to oxidize in catalysts based on noble metals (Papaefthimiou, Ioannides & Verykios, 1997).

The curves of total conversion of ethyl acetate to CO₂ versus the reaction temperature are shown in Figure 7. Temperatures to reach 50% (T₅₀) and 90% (T₉₀) of conversion of VOC to CO₂ are employed as a measure of activity to compare the catalytic behavior among the catalysts. This figure shows the effect of the active phase, given that the oxides that contain manganese show better catalytic behavior than the single Co oxide. This behavior is explained in terms of the OSC results where the manganese oxides feature better redox properties (greater OSC values) than oxide CPCo1.0.

Table 1 lists the T₉₀ values, the OSC, the concentration of the ¹⁶O₂ species and the quantity of α oxygen species desorbed at temperatures lower than 400°C. On the basis of these results, it can be established that high OSC values evidence the presence of more labile and reactive oxygen species capable of undergoing redox cycles and a high percentage of ¹⁶O₂ would show a great oxygen mobility.

5. RESULTS ANALYSIS

It is accepted in the literature that oxidation processes on oxides can be carried out by means of two mechanisms: suprafacial and intrafacial (Morales et al., 2007; Yamazoe & Teraoka, 1990; Zhang et al., 2012) . In the suprafacial mechanism the process is carried out at low temperatures (< 400°C) where the α adsorbed oxygen species play an important role in the catalytic activity, whereas in the intrafacial mechanism higher temperatures are required (> 400°C), which is also related to the redox properties and the mobility of oxygen species close to the surface and lattice oxygens represented like β species.

The presence of α and β species were determined by means of O₂-TPD, OSC and isotopic exchange techniques (these latter for β species) and their participation in the catalytic process was discussed with the T₉₀ values in the oxidation of ethyl acetate.

Figure 7 and Table 1 show that mixed oxides CPMn1.0 and CPCoMn0.5 exhibit the same T₉₀ value (226°C) even though with different quantity of oxygen species, different OSC and oxygen mobility values (Figures 4, 5 and 6). This similar catalytic activity among the manganese-containing oxides can be explained in terms of the participation of the α oxygen (oxygen adsorbed on the surface vacancies) in CPMn1.0 to compensate for the lower redox properties present in this oxide. On the other hand, CPCoMn0.5 has greater quantity of oxygens capable of produce redox cycles (greater OSC value), which are responsible for the oxidation process. Results suggest that in the oxidation of ethyl acetate on manganese mixed oxides, the participation of the surface adsorbed oxygens and the more labile oxygens participating in oxide-reduction cycles play a determining role possibly involving a suprafacial or intrafacial mechanism.

On the other hand, in oxide CPCo1.0 the catalytic behavior is essentially attributed to its high oxygen mobility, involving the participation of the bulk oxygens by means of an intrafacial mechanism. However, as shown in Table 1, even though this oxide presents the greatest oxygen mobility (represented by a greater quantity of ¹⁶O₂ exchanged) it is not necessarily the most active catalyst, therefore requiring the existence of optimum oxygen mobility and an acceptable capacity to participate in redox cycles or the presence of α oxygen species that participate in the oxidation reaction of VOCs.

From the results we can conclude that even though the three mixed oxides are derived from hydrotalcite type precursors, the oxygen species involved in the catalytic process depend on the oxygen vacancies generated, and the existent oxygen mobility, redox cycles and active phases.

6. CONCLUSION

The manganese-containing oxides (CPMn1.0 and CPCoMn0.5) show greater OSC values than the oxide containing single Co and therefore exhibit better catalytic behavior in the oxidation of the ester. The results demonstrated the joint participation of the adsorbed oxygens (α) and the redox properties of the oxides in the VOC oxidation given that even though CPMn1.0 (single manganese) shows lower redox properties than the Co-Mn oxide, the presence of a greater quantity of α species contribute to its catalytic behavior. The oxygen species involved in the catalytic process are dependent on the active phase employed, the oxygen vacancies, the oxygen mobility and the redox properties generated.

The authors thank DIB projects, Hermes codes 14785 and 15056 of Universidad Nacional de Colombia.

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AUTHORS

María-Haidy Castaño-Robayo
Affiliation: Universidad Nacional de Colombia ]]> Chemist, Universidad Nacional de Colombia
Ph.D. in Chemical Sciences, Universidad Nacional de Colombia
e-mail: mhcastanor@unal.edu.co

Rafael Molina-Gallego
Affiliation: Universidad Nacional de Colombia
Chemist, Universidad Nacional de Colombia
Ph.D. in Applied Natural Sciences, Université Catholique de Louvain
e-mail: ramolinag@unal.edu.co

Sonia Moreno-Guáqueta
Affiliation: Universidad Nacional de Colombia ]]> Chemist, Universidad Nacional de Colombia
Ph.D. in Applied Natural Sciences, Université Catholique de Louvain
e-mail: smorenog@unal.edu.co