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Oxidative coupling of bio-alcohols mixture over hierarchically porous perovskite catalysts for sustainable acrolein production

The acrolein production from bio-alcohols methanol and ethanol mixtures using AMnO3 (since A = Ba and/or Sr) perovskite catalysts was studied. All the prepared samples were characterized by XRD, XPS, N2 sorption, FTIR, Raman spectroscopy, TEM, SEM, TGA, and NH3–CO2-TPD. The catalytic oxidation reaction to produce acrolein has occurred via two steps, the alcohols are firstly oxidized to corresponding aldehydes, and then the aldol is coupled with the produced aldehydes. The prepared perovskite samples were modified by doping A (Sr) position with (Ba) to improve the aldol condensation. The most catalytic performance was achieved using the BaSrMnO3 sample in which the acrolein selectivity reached 62% (T = 300 °C, MetOH/EtOH = 1, LHSV = 10 h−1). The increase in acrolein production may be related to the high tendency of BaSrMnO3 toward C–C coupling formation. The C–C tendency attributes to that modification have occurred in acid/base sites because of metal substitution.


Introduction
Acrolein (CH 2 ]CHCHO) is a signicant chemical intermediate with high reactivity due to a combination of vinyl and carbonyl groups. 1 Acrolein is used in many syntheses for high-value industrial products, including acrylic resins, super absorbing polymers, detergents, as well as for feed applications such as methionine and biocides, and so forth. 2 The rst commercial method for acrolein production was an aldol condensation of acetaldehyde and formaldehyde. In the 1940s, Shell developed this method using copper oxide loaded on silicon carbide as a catalyst. The industrial synthesis of acrolein is primarily carried out through propylene oxidation over bismuth, iron, molybdate, Ni and/or Co and K, including many additives Sb, B, W, or P as multi-metals mixture catalysts to improve the activity and selectivity of the prepared catalysts. Using these catalysts to achieve ca. 99% propylene conversion and high selectivity toward the desired product, acrolein reaches up to 80-90%. 3 So an efficient process for the production of acrolein from renewable resources is most necessary. Accordingly, an alternative to acrolein production using a methanol/ethanol mixture as a feedstock reactant has been investigated via oxidative alcoholic coupling. 4 These feedstocks can be obtained from renewable resources at low prices. Ethanol is already being fermented using three primary sources: agriculture, forestry, and industrial byproducts, while methanol from waste gasication via syngas conversion. 5 In the oxidative alcoholic coupling, the reaction can be carried out in two steps as dened (eqn (1) and (2)), including partially alcohol oxidation followed by aldol condensation to acrolein. 1,6 The reactions preferably occur in one reactor (allowing energy saving) in which all reactions occur simultaneously. CH 3 OH + C 2 H 5 OH + O 2 / HCHO + CH 3 CHO + 2H 2 O (1) Numerous catalysts have been reviewed for the gas-phase aldolization of acetaldehyde and formaldehyde in an O 2 -free environment: mixed oxides, 4 hydrotalcite, 7 zeolites, 8 clays, 9 silica, and alumina. 10 The aldolization reaction is favored by cooperation between the acidic and basic sites (amphoteric catalysts). Therefore, it is essential that balance acidic and basic properties. Lilić et al. 1 deliberated the inuence of acid/base properties of numerous catalysts on the cross-aldolization of acetaldehyde and formaldehyde from a mixture of methanol and ethanol. The authors proposed that the coexistence of basic and acidic sites appears to be the optimal surface conguration for maximizing acrolein production.
Perovskites are complex mixed metallic oxides with the general formula of ABO 3, which have exceptional diversity of physical and chemical properties. These perovskite compounds are ceramic materials with a hexagonal structure and have a space group of P6 3 /mmc with a shared oxygen polyhedron at room temperature. Their structures can expose to tilting of the oxygen octahedrons, which causes a slight distortion of cubic perovskite structures. 11 The defects or even spatial distortion in perovskite structure will be established when A and B elements are doped or substituted with others to form the exible various structure oxides with the formula of A 1Àx A 0 x B y B 0 1Ày O 3Àg (ref. 12) with oen oxygen vacancy (g). The oxygen vacancy formed and improved electronic conductivity because the doping in the A site, while the doping occurs at the B site, can promote catalytic activity. 13 However, a great potential proposed that the oxygen vacancies in the perovskite oxide structures play a prominent role in catalytic reactions since oxygen vacancies are preferential sites for O 2 adsorption.
From this point of view, perovskites showed signicant air pollution abatement via the pollutant catalytic oxidation reaction. Recently, a hexagonal structure SrMnO 3 and SrMnBO 3 (B-Co, Cu) nano perovskite as a catalyst exhibiting high catalytic activity towards soot oxidation, which explained from XPS results (O 1s peak), SrMnCoO 3 , the highest active catalyst up to $ 64% because of having the highest mobility of adsorbed oxygen species. 14 To the best of our knowledge, the only two publications exhibit applications of perovskite as a catalyst for aldol reactions were reported by Torres-Martínez et al., 15 who using alkali tantalates (ATaO 3 , with A ¼ Li, Na, and K) for catalytic aldol condensation of acetone at the gas phase by, and Kleineberg et al. 16 who exhibit the material series A ¼ Ca, Sr and Ba, and B ¼ Ti, Zr, and Ce as a catalyst towards aldol addition of isobutyraldehyde to formaldehyde.
Herein, we present the potential of perovskite as a catalyst towards acrolein production through the simultaneously oxidative coupling of renewable alcohols (ethanol & methanol) followed by aldol condensation of pre-formed aldehydes. The examined perovskites are AMnO 3, where A ¼ Ba or/and Sr are prepared hydrothermally. The prepared perovskite samples were physically and chemically characterized. Their catalytic activity was tested in a xed bed reactor in the gas phase.

Catalyst preparation
The BaMnO 3 (BMO), SrMnO 3 (SMO), and BaSrMnO 3 (BSMO) nanoparticles perovskites were prepared by hydrothermal synthesis. Mn(NO 3 ) 2 $4H 2 O and BaCl 2 $2H 2 O and Sr(NO 3 ) 2 were used as precursor materials; KMnO 4 was used as an oxidizer, while KOH served as a mineralizer. Those precursor materials were dissolved in deionized water, and KOH was added while stirring to adjust the alkalinity of the solution.
The initial molar ratios of the input species were 0.05 KMnO 4 : 0.05 Mn(NO 3 ) 2 : 0.1 (BaCl 2 or Sr(NO 3 ) 2 ): 0.035 KOH for preparing BaMnO 3 (BMO) or SrMnO 3 (SMO). While for Ba 0.5 -Sr 0.5 MnO 3 (BSMO), the initial molar ratios of the input species were 0.05 KMnO 4 : 0.05 Mn(NO 3 ) 2 : (0.05 BaCl 2 and 0.05 Sr(NO 3 ) 2 ): 0.035 KOH. The preparation reaction was done mainly in a Teon vessel. The Teon vessel was lled to 80% of its volume, and then this vessel was placed in the stainless-steel container (autoclave). The crystallization reaction occurred at 270 C for 30 hours; aer the preparation, the autoclave was cooled in air and depressurized. The solid products were washed with deionized water and dried in an oven at 100 C overnight. A nano perovskite powder was nally obtained.

Catalyst characterization
The crystallographic structure and chemical composition of the prepared perovskites were investigated using X-ray powder diffraction (XRD) carried out on Shimadzu XD-1 diffractometer in 2q range between 20 and 80 with Cu Ka radiation (l ¼ 1.54056 A). By employing the well-known Scherrer relation (eqn (3)), the average crystallite size of perovskite samples can be calculated.
D is the crystal diameter, k is constant, l is the wavelength of Xrays used for diffraction, q is Bragg's angle in degrees, and b is the full width at half maxima peak height in radians. The morphology of the samples was characterized by highresolution transmission electron microscopy (HR-TEM) spectroscopy. The TEM images were obtained on a JEOL 2100F operating at 200 kV. The prepared samples were suspended in ethanol for about 30 min under ultrasonic treatment, then depositing on carbon-lm-coated copper grids. N 2 adsorptiondesorption isotherms and pore size distribution were derived from the low-temperature nitrogen (À196 C) on a gas sorption analyzer Quantachrome NOVA2000, USA. The samples were evacuated at 350 C for 24 h before nitrogen adsorption. The coke content of the used catalysts was determined using thermal gravimetric analysis (TGA) on SDTQ-600 (TA-USA) Thermo Balance instrument. The infrared absorption spectra are presented (at 25 C) for characterizing the functional groups in the frequency range from 400-4000 cm À1 with a resolution of 4 cm À1 on the (Bruker Tensor-27, Germany). SEM analysis was performed on Carl Zeiss (Germany) to understand the surface morphological properties of the samples, and also, atomic elemental compositions (%) were estimated from EDS analysis. X-ray photoelectron spectroscopy (XPS) analysis was undertaken by Al-Ka micro-focused monochromator XPS spectrometer.
The structure of the prepared perovskite samples can be tuned in numerous substitutes by other cations. However, perovskites stability is determined by the Goldschmidt tolerance factor 17 (eqn (4)).
r A , r B and r O represent the ionic radii of A and B cations and O anion of ABO 3 -perovskite compounds.

Catalytic activity
The catalytic activity of the prepared perovskite samples was carried out in a continuous ow system comprising a quartz tubular reactor operating under atmospheric pressure on using 0.2 g of the prepared sample, which was diluted with 0.2 g of silicon carbide. A methanol/ethanol mixture (1 : 1) was fed into the reactor by a dosing pump with a ow rate of 2 ml per hour using nitrogen as carrier gas (45 cm 3 (NTP) per min). The reaction temperature was varied between 150 and 300 C. The products such as acrolein, formaldehyde, acetaldehyde were analyzed using off-line ame ionization detection (FID) gas chromatography.

Structural analysis
The XRD pattern for the prepared samples BaMnO 3 , SrMnO 3, and Ba 0.5 Sr 0.5 MnO 3 ( Fig. 1) shows represent well-determine sharp peaks, which means that the prepared samples are crystalline in agreement with JCPDS standard data le no. 0260168, 18 while SrMnO 3 and Ba 0.5 Sr 0.5 MnO 3 structure indexed to JCPDS standard data le no. 010841612. 19 The diffraction patterns of Ba 0.5 Sr 0.5 MnO 3 displays the light enlargement of the prominent peaks, and the main peak position 2q ($32.8 ) progressively shi to lower 2q values ($32.4 ), which conrmed the replacement of Sr 2+ with Ba 2+ . 19 The intensity peaks in the Ba 0.5 Sr 0.5 MnO 3 sample illustrate mixed phases, i.e., not totally in the hexagonal structure. Other distorted forms (orthorhombic, octahedral, tetragonal) may be possible in this case. Such structural variations are expected since the greater Ba 2+ ion (1.47 A) in the perovskite structure replaces the smaller Sr 2+ ion (1.13 A), which results in increased cell volumes and decreased crystallinity, which also conrms the substitution of ions. 20 The crystal size quantied by Scherrer's equation is 25 nm for BaMnO 3 and 39 nm for SrMnO 3, which decreases to 21 nm for Ba 0.5 Sr 0.5 MnO 3 catalyst (Table 1). Based on the tolerance factor (t) of BaMnO 3 , SrMnO 3 , and Ba 0.5 Sr 0.5 MnO 3 , which equals 1.097, 1.033, and 0.942, respectively, these structures can be explained as follows: if (t) is equal to one, the geometry of the composition is ideal cubic perovskite. Nevertheless, if (t) is minor larger than unity, as in BMO and SMO, hexagonal perovskite structures are formed. Cations in the A site are enlarged because there is an increasing amount of face-shared links between octahedrons of MnO 6 . The bond angle between Mn-O-Mn face-shared linkages is detected to be 90 in these structures. In case t was slightly decreasing from unity as in BSMO, as a consequence of twisting and sloping alterations of MnO 6 octahedron, Mn-O-Mn bond angle decreases 180 to recompense small A-site cations. 21,22 Fig. 2 displays the infrared spectra of the synthesized perovskites. The peak seen in the wavenumber range 450-492 cm À1 corresponds to the bending mode, which is sensitive to change in the Mn-O-Mn bond angles. The peak assigned in the range 505-786 cm À1 is attributed to the stretching vibration of metal oxide (M-O) bonds in BMO. The peak at 1590 cm À1 can be related to the H-O-H bending vibration. The main absorption band around 600 cm À1 corresponds to the stretching of the metal-oxygen bond in the perovskite, which involves the internal motion of a change in Mn-O-Mn bond length in MnO 6 octahedral, which certied the formation of metal oxide framework in the perovskites. The three peaks at 760, 696, and 510 cm À1 are ascribed to the stretching vibration of metal-oxide (M-O) bonds in SMO, matching well with the published literature. The peak centered at 1639-1649 cm À1 is due to the bending vibration of aerially adsorbed water. The weak broadband visible around 3447-3498 cm À1 indicates the stretching vibration of hydroxyl groups (OH or H 2 O) with an intramolecular hydrogen bond. The FTIR spectra for BSMO perovskite show a similar SMO pattern, with an increase in the intensity of the vibration frequency at 1628 cm À1 which is characteristic of Ba-O stretching mode, and the band at 850 cm À1 attributed to the stretching vibration of metal oxide (M-O) bonds in BSMO sample. Also, the broadening and increasing intensity of the peaks in the range of (400-600 cm À1 ) the position of the stretching vibration of metal oxide (M-O). That is conrming the doping of SMO by Ba ion. 23 The structure of the prepared samples was also conrmed via Raman spectroscopy in the wavenumber range of 200-800 cm À1 (Fig. 3) claried the behavior of the Raman intensity in the spectral ranges of 370-445 cm À1 and 610-770 cm À1 which are characteristic for bonds of Mn-O-Mn. In BSMO, 695 cm À1 indicating Ba-O-Ba bonds. These data are matching well with previously reported papers. 24 Thus, the FTIR and Raman investigations are agreed well with the results of XRD.
X-ray photoelectron spectroscopy (XPS) is a valuable tool to identify the composition and oxidation state of the ions in the perovskite structures. XPS patterns of BMO & SMO samples  2 eV attribute to Ba 3d 5/2 due to Ba 2+ in the perovskite lattice and Ba 3d 3/2 related to the surface oxide/hydroxide, respectively. The two peaks at 131.61 & 133.38 eV for the SMO sample identied the binding energies for Sr 3d 5/2 and Sr3d 3/2 . These values established the presence of Sr 2+ species in the lattice and the SrO/Sr(OH) 2 structure on the surface, respectively. This means that Ba and Sr in the samples display +2 valence on the catalyst surface. 25,26 On the other hand, the binding energy position for the BMSO sample is slightly shied may be related to the partial substitution of the lower electronegative element (Sr: 0.95) with a higher one (Ba: 0.89). At the same time, the Ba 3d lines are not affected, which emphasized that substitution occurs in SMO, not in BMO lattice, in good agreements with XRD data.
From the literature, the assignment of the manganese oxidation states by XPS is a difficult task. 27 In Fig. 5, the peak maximum of the Mn 2p 3/2 transition suggests the occurrence of Mn 3+ and Mn 4+ in all the prepared samples. The Mn 2p 3/2 band has been deconvoluted, and peaks at around 641.3 eV and 643.1 eV are ascribed to Mn 3+ and Mn 4+ , respectively. It affirms the presence of +3 and +4 valence states of Mn on the surface of all samples. From the area of the corresponding peaks, the ratio Mn 4+ /Mn 3+ was calculated and be lower than 1 for all the samples indicate that Mn 3+ is the main oxidation state, the Mn 4+ /Mn 3+ ratio for BMSO is the lowest value, which refers to the substitution of Ba with Sr promotes an increase of Mn 3+ amount. Based on the BaMnO 3 & SrMnO 3 stoichiometric formula, Mn 4+ has to be the predominant manganese oxidation state in the samples. Consequently, an increase of the Mn 4+ amount would be expected to compensate for the additional defect of the positive charge (due to Sr substitution). However, XPS results reveal the opposite effect as the Mn 3+ amount increase. Thus, electroneutrality must be achieved by generating oxygen vacancies by forming a non-stoichiometric (oxygen-decient) perovskite ABO 3Àa . Furthermore, the highest amount of oxygen vacancies must be generated in the BSMO sample as it signied the lowest Mn 4+ /Mn 3+ ratio.     29 We can also be observed that the release of oxygen species is attributable to variations in electron negativity between metal and oxygen which means that the metal and oxygen interactions are bindings. 30 For alcohol partial oxidation reactions to corresponding aldehydes, higher content of (O 2 , O À ) species is needed for that low-temperature reactions. As shown in Table 1, the percentages quantity of active oxygen of the samples, BMO, SMO, and BSMO, are found to be 51%, 40%, and 53%, respectively. It is claried that the calculated amount of active oxygen species was higher for doped samples than the undoped ones. La 1Àx K x Co 1Ày Cu y O 3 catalysts with A and B cations substitution were tested, resulting in a rise in the surface oxygen groups correlated with oxygen vacancy generation. 31 Furthermore, Zhan and the team found that when lanthanum substitutes for LaMn 0.5 Cu 0.5 O 3 perovskite, an increase in the O ads /O L ratio suggests a greater amount of oxygen defects catalysts. 32 Similarly, the lower amount value of the O L /(Ba + Sr + Mn) ratio increases the oxygen vacancies in prepared perovskites. In addition, BSMO catalyst is the perovskite with the highest number of structural defects, as is expected based on the analysis of the Mn 2p 3/2 spectra. Thus, the sample BSMO might be an excellent catalytic activity because of its excellent redox properties and higher surface-chemisorbed oxygen species.
The textural parameters of the prepared nanostructured materials are listed in (Table 1 and Fig. 6) represented that all samples exhibited that a classical type IV isotherm, which was the characteristic of the mesoporous structure. The presence of H2 type hysteresis loops in the isotherms suggested the appearance of ink-bottle pores with narrow entrances and large cavities. The mean diameter and total volume of the nanostructures (Table 1) in the range of 1-10 nm by using the BJH analysis indicating the porous mesoporous structure.
The morphology and microstructure of the sample were more explored by TEM (Fig. 7). Fig. 7A and B represent TEM images of the hierarchically nanostructured (BMO and SMO) perovskite samples, in which one can observe an individual nanorod with a smooth surface. In contrast, Fig. 7C (BSMO) shows the edges of the nanosheets built up by nanorods. That is similar to, 33 who observed the same behavior on preparing hierarchically porous LaFeO 3 via the hydrothermal method.
The number, strength, and strength distribution of acid/ base sites were analyzed by TPD of NH 3 and CO 2 probe molecules, respectively. It is important to note that ammonia is suitable to quantify Brønsted acid sites (transfer of a proton from surface hydroxyls) and Lewis sites (coordination with an electron-decient atom such as a metal cation).
According to previous reports, 34 the NH 3 molecules coordinated to the Lewis acid sites exhibit higher thermal stability than the NH 4 + ions bound to the Brønsted acid sites; herein, the mid-strong acid sites could mainly be the Lewis acid sites. For BMO, two desorption peaks were detected and attributed to the mid-strong acid sites (200-500 C). Similarly, the number of CO 2 desorption peaks ( Fig. 8) was observed to be the same as the number of NH 3 desorption peaks on BaMnO 3 . The total amount of acidity and basicity are 71 and 79 mmol g À1 , respectively. So, catalysts displayed both acidic and basic characters. For the SMO and BSMO, the ammonia desorption peaks position 636.5 and 619.9, and the total acidity is 41 and 32 mmol g À1 , respectively. By comparing the amount of NH 3 desorption, it was concluded that the introduction of Ba played a positive effect on providing mid-strong acid sites. It is worth noting that BSMO has the least amount of strong acidic sites of all the prepared samples. Indeed, as displayed in Fig. 9, the O 1s binding energy (from XPS) decreases with an increasing number of acidic sites per surface area square meters. However, lower O 1s binding energy indicates an electron-rich element, which means more basic sites agree with Védrine et al., 35 proposal. All these results approve the amphoteric character of all samples.

Catalytic activity
The catalytic activity of prepared perovskite samples was evaluated using a mixture of bio-alcohols methanol and ethanol in the presence of carrier (N 2 ) with conditions LHSV ¼ 10 h À1 , temperature range ¼ 150-300 C, MeOH/EtOH ¼ 1 molar ratio. The effect of temperature on mixed alcohol conversion, product distribution, and selectivity for prepared samples is graphically illustrated in Fig. 10-12.
In our study, reaction conditions, a wide range of different reaction products of methanol and ethanol conversion can be classied as follows: (a) C-C coupling (e.g., C 3+ alcohols; C 3+ aldehydes; C 3+ esters); (b) non-C-C coupling (e.g., formaldehyde, acetaldehyde, ethyl acetate). From the data in the gures, we can see that an increase in temperature from 150 to 300 C affects pointedly on methanol and ethanol conversions. Methanol conversion was reached 64, 63.2, 90.2%, while ethanol conversion was reached 74, 73.4, 98.4% using BMO, SMO, and BSMO samples, respectively. As claried, a good correlation between the conversion of alcohols and metal composition on the perovskite surfaces. The most essential obtained products are acrolein, acetaldehyde, and formaldehyde. In addition to traces of other tiny products. The low carbon balance (in the 57-93%) results from coke deposition on the catalyst surface. 1 The absence of crotonaldehyde, acetaldehyde via self-aldolization (2CH 3 -CHO / CH 3 -CH-CHO), may be explained as follows: from thermodynamic view at a temperature range between 150 and 400. Acrolein is the more favored product formed than crotonaldehyde. Due to alcohol oxidation to aldehydes, the partial pressure of water vapor is even higher, inhibiting the self-aldolization reaction, and a pronounced product acrolein was formed. 1 In other words, in the absence of oxygen, as in our study, both acetaldehyde and formaldehyde were adsorbed (creating two carbocations) and further reacted to form acrolein.
There is a positive correlation between catalytic activity and Mn 4+ /Mn 3+ ratio on the surface (obtained from XPS). Mn 4+ acts as stronger Lewis acids than Mn 3+ and weak Lewis acid sites are required for this reaction. Therefore, BSMO with a low Mn 4+ / Mn 3+ ratio exhibits high activity while BMO low catalytic activity. The loss of an electron (Mn 3+ ) results in a signicant migration of the unstable interstitial oxygen, which escapes from the lattice and transforms into active oxygen (O À ). Similarly, doping of Sr 2+ in a LaMnO 3 perovskite has been described to present a mixture Mn 3+ and Mn 4+ states, where Mn 3+ -O bonds have different ionic strength than Mn 4+ -O bonds and consequently formed oxygen vacancies. 36 Recent studies demonstrate that basic sites are required for catalyzing crosscondensation because they can activate acetaldehyde by abstracting a hydrogen atom from the a-position of carbonyl. 6 In addition, weakly acidic sites can activate formaldehyde by increasing the C atom's electronegativity. 9 Another report used molybdenum dopped copper ferrite for oxidative coupling of   primary alcohols, demonstrate that the aldehyde formation by dehydrogenation or by oxidation needs the presence of moderately basic sites (M 2+ -O 2À ). 37 For selectivity, acidic sites exhibit a strong inuence on selectivity; the cross-selectivity seems to be controlled by acidity rather than basicity. On the other hand, using amphoteric catalysts as in our work, acrolein production is improved, and carbon oxides production is reduced, consequently allowing the catalyst to work at higher temperatures. 8 As mentioned in TPD analysis, the prepared perovskites have acidic and basic sites and are considered amphoteric catalysts. BSMO exhibits a high basic character which explains its high catalytic activity rather than BMO and SMO. BSMO displays moderate acidic and basicity character among the others, which elucidate high acrolein selectivity at relatively low temperature (200 and 250 C), which reached $52 and 60%, respectively.
The formation of acrolein via cross condensation between formaldehyde and acetaldehyde can be summarized via the following equations (eqn (5)-(8)):    The methyl ethyl ether selectivity is higher at low temperatures. The catalyst order BMO > BSMO > SMO decreases with increasing temperature, in which dehydration reactions occur faster than other reactions. One alcohol molecule is adsorbed on the weak Lewis acid sites via the oxygen of the OH group. The second alcohol molecule is adsorbed on the strong Lewis basic site via the H of the OH group, resulting in forming an alkoxide on the surface, which reacts to form corresponding ether. 38 On the contrary, methyl acetate formation increases with increasing temperature. Indeed, the BSMO has a higher selectivity for methyl acetate, reaching 18% at 300 C. The selectivity is explained by the formed acetaldehyde with the newly formed methanol molecule via oxidative esterication (non-C-C coupling) to form methyl acetate.
For all samples, methyl acetate reached the plateau or slowly increased in selectivity with increasing temperature due to complete conversion of methanol as in BSMO or methanol decomposition favored at high temperatures. The increase in the selectivity of propanol and butanol alcohols is consistent with their involvement in esterication reactions, as evidenced by the concurrent increase in the selectivity of ester. Moreover, the presence of aldehyde accelerates the ester formation and, at the same time, prevents the oxidation of the secondary aldehyde to acid. Fig. 13 illustrates that the doping of SMO with Ba 2+ in BSMO attained the highest rate of C-C coupling products relative to non-C-C coupling at 250 C. In conclusion, the observed results suggested that the prepared BMO, SMO, and BSMO samples are more favorable for C-C coupling products with low production of non-C-C coupling and negligible CO x byproducts.

Characterization of used catalysts
The types of carbon species formed on the used BMO, SMO, and BSMO catalysts were examined using a thermogravimetric analyzer (TGA). Their TGA proles and derivatives are shown in (Fig. 14). The initial loss below 300 C in all catalysts is due to removing moisture, and CO 2 adsorbed, followed by the loss of   easily oxidized carbonaceous species. 39 The used BSMO catalysts prole exhibits an exothermic peak at around 415 C, attributed to physisorbed carbonaceous products (socore). In comparison, BMO and SMO prole exhibits the peaks at higher temperature 540 and 590 C respectively. This associated with lamentous hard coke followed a major decrease in the sample's weight ($1.5 and 2%), showed the gasication of the bulky carbonaceous species or hard coke, generating CO and CO 2 (CO x ). 40 In addition, the peak at the high-temperature range of 600-700 C is attributing to graphitic carbon species. This graphitic carbon is a non-reactive coke that infrequently reacts with oxygen. 41 Fig . 15 shows the FT-IR spectra of fresh and used aer oxidative coupling reaction of methanol and ethanol. There is no noticeable difference in the spectra for the fresh and used catalysts. The intensities of all bands decreased, probably due to coke deposition on the perovskite surface. This behavior is not found to a great extent in the case of a BSMO catalyst. The coke formation could further verify this, as shown in the TG curves.
SEM images obtained at 4000 magnication are shown in (Fig. 16A), revealing the effect of the change in A element in ABO 3 perovskite on uniformity, homogeneity, and surface morphology of the perovskite samples. All samples show good homogeneity having almost uniform shapes. The grain boundaries are sharp, with most of the grains have nanorods with a diameter in the nanometer range and a length of 2 mm. The average grain diameter for the BSMO is the least one of the fresh catalysts showing that grain size is highly doping dependent. Most grain's plane and sharp faces also show the crystallographic texture and well-oriented growth samples. 22 The images also show the walls of macropores, which were assembled by a large number of nanoparticles with the formation of nanovoids, and it was apparent conrm that perovskite samples possessed hierarchically pore structure; this would make reactants more diffuse and increase the contact effectiveness between reactants and catalysts so that improved catalytic performance could be achieved. 33 All surfaces have been rearranged to take on more regular forms aer the reaction as shown in (Fig. 16B). In contrast, SMO has modied all surface morphologies to reect further particle deformation and agglomeration, mainly because of the problematic reaction conditions during the process, so that it generated no aggregates of regular shapes or structures.
EDX is a technique used to identify the elemental composition of the typical product. The EDX spectra established in all the samples have no impurity element present in the samples ( Fig. 17A and B). The elements present in the respective spectra are correct stoichiometric ratios, precisely following empirical formulas of the corresponding composition. The EDX results prove that only three types of elements, Ba or Sr, Mn, and O, in the BMO and SMO samples. And four elements Ba, Sr, Mn, and O in the BSMO sample. There are some minor peaks related to C (in fresh catalyst) because of the sticking tape used to hold the samples in place. It related the carbon peaks that appear in the EDX spectra to coke deposition, 43 as conrmed in TGA and FTIR analysis for used catalysts.   Table 2 shows the comparison of different catalysts towards acrolein selectivity via oxidative coupling of bio-alcohols mixture.

Conclusion
The physico-chemical properties of hierarchically porous perovskite catalysts were determined by XRD, FTIR, Raman spectroscopy, XPS, N 2 sorption, TEM, SEM, TGA, and NH 3 -CO 2 -TPD. Also, the role of A (Ba or/and Sr) position variation in AMnO 3 perovskite catalysts has been studied in the oxidative coupling of primary alcohols performed at atmospheric pressure using a methanol/ethanol equal 1. These characteristics were associated with catalytic activities for the aldolization reaction (to form acrolein), promoted by coordination between the acids and basic sites. The balance of acidic and basic properties of the catalysts is critical in the production of acrolein. Of the catalysts studied, BaSrMnO 3 demonstrated the highest performance, followed by SrMnO 3 and BaMnO 3 . The high activity was attributed to the signicantly faster formation of C-C bonds in BaSrMnO 3 than in other materials. Acrolein, acetaldehyde, methanol, ethanol were the main products found with each catalytic test. Crotonaldehyde was not formed during the reaction, indicating more resistance to self-condensation kinetics than the cross-condensation reaction under current reaction conditions. In general conclusion, these catalysts propose promising yields of acrolein, making it a superb choice to be effective in a viable process.