Synthesis of Chalcone Using LDH / Graphene Nanocatalysts of Different Compositions

Layered double hydroxides (LDH) or their derived mixed oxides present marked acid-base properties useful in catalysis, but they are generally agglomerated, inducing weak accessibility to the active sites. In the search for improving dispersion and accessibility of the active sites and for controlling the hydrophilic/hydrophobic balance in the catalysts, nanocomposite materials appear among the most attractive. In this study, a series of nanocomposites composed of LDH and reduced graphene oxide (rGO), were successfully obtained by direct coprecipitation and investigated as base catalysts for the Claisen–Schmidt condensation reaction between acetophenone and benzaldehyde. After activation, the LDH-rGO nanocomposites exhibited improved catalytic properties compared to bare LDH. Moreover, they reveal great versatility to tune the selectivity through their composition and the nature or the absence of solvent. This is due to the enhanced basicity of the nanocomposites as the LDH content increases which is assigned to the higher dispersion of the nanoplatelets in comparison to bulk LDH. Lewis-type basic sites of higher strength and accessibility are thus created. The nature of the solvent mainly acts through its acidity able to poison the basic sites of the nanocatalysts.


Introduction
The design of hybrid materials with multifunctional properties through the combination of various building blocks is a growing topic in material science.Considerable attention is thus given to the development of nanohybrid materials composed of layered double hydroxides (LDH) and carbon based materials [1] such as carbon nanotubes (CNT), carbon nanofibers (CNF), multiwalled carbon nanotubes (MWCNT), graphene (G) and chemically modified graphene such as graphene oxide (GO) [2].The catalysts obtained by self-assembly of LDHs and (nano)carbon supports exhibit higher mechanical strength, surface area, thermal conductivity and chemical reactivity than the corresponding constituents.For instance, LDH/carbon fibers (CF) nanocomposites obtained by growing MgAl LDHs in situ on CF were efficient catalysts for the transesterification reaction of glycerol with diethyl carbonate into glycerol carbonate [3].LDH crystals deposited inside a mesoporous carbon material (CMK-41) were highly active catalysts in Claisen-Schmidt condensation [4].Winter et al. [5] and, more recently, Álvarez et al. [6] investigated the catalytic activity of MgAl-LDH/CNF nanocomposites.Their specific activities were more than four and hundred times higher in the acetone self-condensation and the glycerol transesterification with diethyl carbonate, respectively, than the unsupported LDHs.Similarly, MgAl-LDHs supported on MWCNT showed enhanced activity in the acetone self-condensation [7].The common features of these hybrid materials are a small particle size and a good dispersion of the LDH active phase, together with other factors such as tunable polarity.It is believed that the immobilization of LDH on the surface of GO or reduced graphene oxide (rGO) support would produce highly efficient nanocatalysts.Indeed, the large surface area of the support allows for high dispersion of the LDH particles and thus of the active sites, and its high electrical conductivity will enhance the carrier mobility and improve the electron-hole separation efficiency of LDH.This latter feature is interesting for photocatalytic applications.The LDH-G, LDH-GO and LDH-rGO nanocomposites are used in various fields such as supercapacitors, water splitting, electrochemistry and photocatalysis among others [8].However, applications involving C-C bond formation of great interest for fine chemistry applications are reported in much lesser extent.Ahmed et al. [9] reported the activity of CuCo-LDH/rGO materials in the C-C coupling via Ullmann reaction, where the use of transition metal catalysts is required.In the same time, we presented a new application of MgAl-LDH/rGO structures as active solid base catalysts in C-C bond formation reaction [10].In it, we have reported, that a nanocomposite with LDH:rGO mass ratio of 10 achieves the condensation of acetone at 0 • C with about 20% yield of diacetone alcohol, only slightly below the thermodynamic equilibrium (23.1%).An influence of the synthesis method on the structure-activity relationship has been evidenced.
The Claisen-Schmidt condensation reaction between acetophenone and benzaldehyde leading to chalcone is a valuable C-C bond-forming reaction, usually achieved with basic catalysts.This reaction is of great interest because a wide range of applications of chalcones, which are natural precursors of open chain flavonoids, are considered for the synthesis of many pharmaceutical compounds, fragrances, etc.Moreover, their biological properties include antibacterial, anti-inflammatory, antimalarial, antifungal, antiviral, antioxidant, mutagenic and cytotoxic activities, among the most significant [11].Chalcones can exist in two isomeric forms, cis and trans, the trans-chalcone exhibiting special anti-cancerous properties [12,13].Chalcones have been synthesized using different type of catalysts, solvents and temperatures.Various base catalysts were used such as NaOH-EtOH, or solids such as K 2 CO 3 , barium hydroxide, alumina, MgO, alkali-exchanged zeolites, hydroxyapatites, activated carbons, mixed oxides obtained from LDH precursors and carbon supported LDHs [11][12][13][14][15][16][17] covering a wide range of basic strength.However, the selectivity to chalcone is generally low due to several side reactions leading particularly to Michael addition product.Interesting results were obtained using calcined-rehydrated Mg/Al LDH catalysts known to contain intercalated OH -anions acting as Brønsted basic sites.Lopez et al. [18] carried out the reaction at 0 • C in dimethylformamide (DMF) and reach 80% chalcone yield after 3 h.On the other hand, the reaction has been performed without solvent by Climent et al. [15] reaching 98% yield of trans-chalcone after 4 h at 150 • C.These calcined-rehydrated Mg/Al LDH catalysts were by far more active than the non-rehydrated Mg(Al)O mixed oxides obtained from calcined Mg/Al LDHs containing mainly O 2− -Mn + acid-base pairs.Using such mixed oxide Guida et al. [19] reported 20% chalcone yield after 24 h when the reaction was carried out at 110 • C in ethanol.However, a main drawback of the calcined-rehydrated LDHs is that the rehydration step is a delicate process.Therefore, the LDH/rGO nanocomposites with highly dispersed Mg(Al)O platelets of low size leading to a high density of low-coordinated O 2− sites which are able to achieve the self-condensation of acetone appear very attractive for the Claisen-Schmidt condensation reaction.
Here, we studied the condensation reaction between acetophenone and benzaldehyde using LDH/rGO nanocatalysts whose LDH:rGO mass ratio has been varied between 0.5 and 20 in order to adjust the textural and the basic properties.Chalcone yields were particularly followed to determine the influence of the dispersion and of the low platelet sizes of the activated LDH phase in the LDH/rGO nanocatalysts in comparison to the bulk Mg(Al)O mixed oxide.As the influence of the solvent could be determinant, solvents of different nature have been investigated.Moreover, with the aim to develop a cleaner process, the reaction has been also studied in the absence of solvent.

Synthesis of GO
GO is commonly used as an easily water-dispersible precursor to G or rGO.GO was synthesized using a modified Hummers method [20].Typically, 10 g of natural graphite and 5 g of NaNO 3 were added to 230 mL of H 2 SO 4 .The temperature of the mixture was kept at 5 • C and then 30 g of KMnO 4 were slowly added into the suspension.After 30 min, the temperature was increased to 35 • C and the mixture was kept for another 30 min after which 460 mL of Milli-Q water was added.Then, the temperature was increased to 90 • C and the reaction was maintained for 1 h.The resulted suspension was then diluted with another addition of 700 mL of H 2 O and, then, treated with 30 mL of a 30 wt% H 2 O 2 solution.The mixture was then cooled down to room temperature and repeatedly centrifuged and washed; first with a 5 wt% HCl solution and then with H 2 O until the pH reached ≈ 5.The resulted solid was dried at 40 • C. The GO dispersion in water (2.5 mg mL −1 ) was prepared by submitting the suspension to mechanical stirring for 1 h and subsequent ultrasonic treatment for 1 h to further exfoliate the GO.Stable brown colloidal suspension of GO layers was obtained after this treatment.

Synthesis of LDH-rGO Nanocomposites
The LDH-rGO nanocomposites were synthesized by direct coprecipitation on the GO surface.The required amounts of metallic cationic nitrate salts (Mg(NO 3 ) 2 •6H 2 O and Al(NO 3 ) 3 •9H 2 O, Mg/Al molar ratio = 3) were added, in this case, to 100 mL of GO dispersed in water (2.5 mg•mL −1 ) to obtain LDH-rGO hybrid materials with LDH:GO mass ratios of 0.5:1; 1:1; 2:1; 5:1; 10:1 and 20:1.Subsequently, a 2 M NaOH + 0.5 M Na 2 CO 3 aqueous solution was added to the mixture to fix the pH at 10 under continuous stirring.The resulting dark-brown suspension was aged at 90 • C for 12 h.The basic media and the hydrothermal treatment allowed both the reduction of GO and the coprecipitation of LDH while the solution turned from brown to black.The suspension was centrifuged, washed several times with H 2 O.The samples thus obtained were dried in static air at 80 • C. In the following they were noted as LDH/rGO-x with x representing the LDH:GO mass ratio.

Characterization Techniques
Powder X-ray diffraction measurements (PXRD) were made in a Bruker-AXS D8-Discover diffractometer with a vertical theta-theta goniometer and a Vantec linear detector.Monochromatic Cu Kα radiation was obtained from a copper X-ray tube operated at 40 kV and 40 mA and a Ni monochromator.Data were recorded over a 2θ range of 4-70 • with an angular step of 0.02 • at 10.6 s/step.Specific surface areas were determined by N 2 adsorption at −196 • C using a Micromeritics ASAP 2020 automatic analyzer.Samples were previously degassed in situ at 150 • C under vacuum for 15 h.Surface areas were calculated using the Brunauer-Emmet-Teller (BET) method over a p/p 0 range where a linear relationship was maintained.
Morphology of the samples was analyzed by electron microscopy.Transmission electron microscopy (TEM) was performed in the bright field using a JEOL JEM-2100 instrument at an accelerating voltage of 100 kV.The samples were prepared by dispersing the as-prepared catalysts in ethanol and then drop casting the suspension on a standard 3 mm holey copper grid and letting the ethanol evaporate at room temperature.Images were not filtered or treated by means of digital processing, and they correspond to raw data.
The actual LDH:rGO ratio was measured by thermogravimetric analysis (TGA) using a Perking Elmer Pyris STA 6000.Typically, 5 mg samples were in situ dried at 80 • C for 20 min and then heated from 80 to 900 The basicity measurements were performed by volumetric adsorption of CO 2 with a Micromeritics ASAP 2010 C apparatus in the range 0-100 mmHg at 30 • C. Samples were previously calcined in situ at 450 • C in vacuum for 5 h.After calcination and evacuation of the sample, small increments of CO 2 were introduced.Once the isotherm was achieved, evacuation at 10 −7 Torr was performed and a second CO 2 adsorption was done on the evacuated sample.The difference between the two isotherms allows calculating the amount of irreversibly chemisorbed CO 2 molecules and then to determine more accurately the number of basic sites when not considering physisorbed CO 2 .
Thus, the total number of accessible basic sites was determined by taking the amount of CO 2 chemisorbed at zero pressure (cm 3 /g STP) obtained by extrapolation of the linear part of the second uptake isotherm.

Catalytic Activity Tests
The performance of the activated LDH/rGO nanocatalysts was evaluated in the Claisen-Schmidt condensation reaction between acetophenone and benzaldehyde.Activation of the nanocatalysts was performed by calcination at 450 • C (2 • C min −1 ) under flowing Ar (70 mL•min −1 ) for 5 h.
The Claisen-Schmidt condensation was performed in a 10 mL tube where a benzaldehyde/acetophenone ratio of 1.05 was added, along with the solvent (when used) and a 25% (in weight basis) of freshly activated catalyst.The mixture was stirred for 4 h at 40 • C (otherwise indicated).These operations were carried out under Ar atmosphere in order to exclude contact with atmospheric carbon dioxide.The catalyst was recovered by centrifugation and washed several times with the solvent, and the reaction medium was submitted to reduced pressure to remove the solvent when this was used.The products were both identified and quantified by 1 H-NMR.

Materials Characterization
As displayed in Table 1, the LDH content in the different LDH/rGO nanocomposites determined by TG analysis is close to the nominal values demonstrating the complete coprecipitation of the magnesium and aluminium nitrate salts in presence of GO.
PXRD patterns of the prepared LDH/rGO hybrids are presented in Figure 1A.They display the typical reflections corresponding to 2D LDH materials with particularly the most intense harmonic (003) and (006) reflections in the 2θ range below 30 • .The interlayer distance (d 003 ) of 0.772 nm is consistent with the presence of carbonate anions into the interlayer space provided by the alkaline synthesis solution (NaOH + Na 2 CO 3 ) [22].As could be expected, the intensity and the shape of the LDH peaks depend on the LDH:rGO mass ratio.The intensity of the peaks decreases and the breadth increases with the decrease of the LDH content (Table 1), indicating an apparent decrease of crystallinity.This is in accordance with the behaviour previously reported by Garcia-Gallastegui et al. [23] and assigned not only to the increased GO contribution but mainly to the electrostatic interactions between GO and LDH during synthesis.This interaction influences the nucleation and then the crystallite size of the LDH particles.The absence of the basal reflection at 2θ = 11.3 • , typical of GO, indicates its reduction into rGO upon hydrothermal treatment.This was further confirmed through analysis of bare GO submitted to the same treatment (figure not shown), where a shift is observed from the intense peak at 2θ ~12 • for GO to a broad peak at 25-30 • assigned to rGO.Moreover, the absence of a marked background in the 2θ range 25-35 • in the nanocomposites indicates that the LDH nanoplatelets prevent the restacking of the rGO sheets.This suggests that the two components are intimately in contact and highly dispersed [24].The well-defined (110) and (113) peaks of the LDH structure observed in the high angle region reveal that the structure of the layers is preserved in the nanocomposites.A deeper analysis of these peaks also reveals an increase in the breath with the increase in the rGO content, as previously seen with (003) basal peak, indicating a decrease in crystallinity not only along the xz plane, but also in the xy plane.Crystallite size was calculated by applying the Scherrer equation with (003) basal plane or (110) plane, confirming this assumption (Table 1).That is, the LDH crystallites in the nanocomposite are smaller and less stacked than in bare LDH.In all samples the lattice a parameter of 0.306 nm calculated from the position of the (110) peak (a = 2 d 110 ) is in agreement with a Mg/Al molar ratio of 3 [25].
After calcination at 450 • C the LDH/rGO composite materials lost the hydrotalcite-like layered structure.Figure 1B shows the PXRD patterns of the calcined composites which exhibit different shapes in function of the LDH content as illustrated by the representative LDH/rGO-0.5,LDH/rGO-5 and LDH/rGO-10 materials.Calcined LDH/rGO-5 and LDH/rGO-10 samples show reflections at 2θ ~43 • and 63 • , corresponding to a periclase-like structure (JCPDS 87-0653) typical of a Mg(Al)O mixed oxide obtained by thermal decomposition of Mg/Al LDH.The calcined LDH/rGO-0.5 material presents a broad reflection at 2θ ~25 • corresponding to rGO sheets.The absence of other peaks corresponding to periclase-like structure is due to both the low LDH content in the parent sample and to its high dispersion on the rGO surface.
Textural and structural data of the nanocomposites are reported in Table 1.All nanocomposite samples, as well as the bulk LDH show a type IV adsorption isotherm typical of mesoporous materials with a H4 hysteresis loop (except LDH/rGO-1) corresponding to slit-shaped mesopores which is normally observed in materials with aggregates of plate-like particles.Instead, sample LDH/rGO-1 displays a hysteresis loop of type H 2 , which is typical of either disordered materials or bottleneck constrictions (Figure 2).Remarkably, the specific surface areas varied slightly between 133 and 148 m 2 •g −1 for the nanocomposites with LDH:rGO ratios ranging from 20:1 to 1:1 and are rather similar to that of the bare LDH (140 m 2 •g −1 ).Due to the low surface area presented by rGO, as generally reported [23], a decrease of specific surface area could be expected in the LDH/rGO composite materials with the decrease of LDH content.The rather similar specific surface areas observed suggest, on the contrary, the formation of homogeneous structure in materials with LDH:rGO ≥ 1.Therefore, as the LDH content increases, dispersion of the LDH platelets on the rGO surface may be improved and/or the GO restacking is reduced by the alternative LDH/GO stacking interactions as previously suggested [10,23].The specific surface area decreases to 25 m 2 •g −1 at low LDH content for the LDH/rGO-0.5composite, well below the specific surface area of the bare LDH, accounting for high aggregation of the LDH particles which, in addition, do not hinder the restacking of the GO layers.Textural and structural data of the nanocomposites are reported in Table 1.All nanocomposite samples, as well as the bulk LDH show a type IV adsorption isotherm typical of mesoporous materials with a H4 hysteresis loop (except LDH/rGO-1) corresponding to slit-shaped mesopores which is normally observed in materials with aggregates of plate-like particles.Instead, sample The behaviour observed for the nanocomposites with LDH:rGO ≥ 1 has been also confirmed by SEM and TEM analysis (Figure 3).The samples are indeed constituted by GO or rGO sheets and relatively well dispersed LDH aggregates in contact displaying a house-of-cards-type structure which suggests the formation of mesopores.This is observed especially in those samples with higher LDH content, as previously reported in recent studies [10], while at low LDH content, sample LDH/rGO-1 yet presented a more stacked structure.At very low LDH content, LDH/rGO-0.5 has the lowest specific surface area in the series (25 m 2 •g −1 ) suggesting the formation of a poorly porous material with highly packed LDH and rGO sheets (Figure 4).SEM and TEM analyses indeed confirms such highly packed structure where rGO and LDH phases are in intimate contact, although the existence of completely separated LDH and rGO domains is also clearly seen.The high homogeneity and dispersion of the LDH platelets in contact with rGO in samples with higher LDH content merits to be highlighted.Figure 5 shows HRTEM analysis of sample LDH/rGO-10 where LHD crystals appeared intimately assembled into the rGO.Besides, the lattice-fringe image shows the different phases occurrence.Lattice fringes at 3.5 Å correspond to the (002) crystallographic planes of graphene, whereas straight planes at 2.28 and 1.95 Å corresponds to LDH.The behaviour observed for the nanocomposites with LDH:rGO ≥ 1 has been also confirmed by SEM and TEM analysis (Figure 3).The samples are indeed constituted by GO or rGO sheets and relatively well dispersed LDH aggregates in contact displaying a house-of-cards-type structure which suggests the formation of mesopores.This is observed especially in those samples with higher LDH content, as previously reported in recent studies [10], while at low LDH content, sample LDH/rGO-1 yet presented a more stacked structure.At very low LDH content, LDH/rGO-0.5 has the lowest specific surface area in the series (25 m 2 •g −1 ) suggesting the formation of a poorly porous material with highly packed LDH and rGO sheets (Figure 4).SEM and TEM analyses indeed confirms such highly packed structure where rGO and LDH phases are in intimate contact, although the This suggests that the steadiness of the surface area in non-calcined hybrids may be related (in different extent) to both intrinsic porosity generated by incorporation of LDH in the hybrids as well as interporosity due to the lower stacking degree of both components (i.e., rGO and LDH) forming the nanocomposite.Whereas, the increase in surface area in calcined materials is due to the pore generation produced by gas release during the LDH decomposition upon thermal treatment confirmed by XRD (Figure 1).2).This is in accordance with earlier studies on basicity characterization of LDH/rGO nanocomposites [10,23,26].
In the analysis conditions of our experiments, the CO2 adsorption capacity of the bare rGO was found negligible.It is notable that CO2 adsorption capacity of sample LDH/rGO-0.5 was around two times lower than that reached by the activated bare LDH and LDH/rGO-1 samples.This is consistent with the morphology and texture of LDH/rGO-0.5 giving rise to low accessibility of the probe to the basic sites.On the other hand, the CO2 adsorption capacity of the samples having the highest LDH content, i.e.LDH/rGO-10 and LDH/rGO-20 is two-fold higher than that reached by the calcined LDH characterization of LDH/rGO nanocomposites [10,23,26].

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In the analysis conditions of our experiments, the CO2 adsorption capacity of the bare rGO was This suggests that the steadiness of the surface area in non-calcined hybrids may be related (in different extent) to both intrinsic porosity generated by incorporation of LDH in the hybrids as well as interporosity due to the lower stacking degree of both components (i.e., rGO and LDH) forming the nanocomposite.Whereas, the increase in surface area in calcined materials is due to the pore generation produced by gas release during the LDH decomposition upon thermal treatment confirmed by XRD (Figure 1).
Volumetric adsorption of CO 2 at low pressure was applied to determine the number of basic sites on the LDH/rGO nanocomposites activated by in situ calcination at 450 • C. The amount of CO 2 adsorbed and then the number of basic sites significantly increases from 52 to 265 µmol•g −1 with the LDH content in the nanocomposites (Table 2).This is in accordance with earlier studies on basicity characterization of LDH/rGO nanocomposites [10,23,26].
In the analysis conditions of our experiments, the CO 2 adsorption capacity of the bare rGO was found negligible.It is notable that CO 2 adsorption capacity of sample LDH/rGO-0.5 was around two times lower than that reached by the activated bare LDH and LDH/rGO-1 samples.This is consistent with the morphology and texture of LDH/rGO-0.5 giving rise to low accessibility of the probe to the basic sites.On the other hand, the CO 2 adsorption capacity of the samples having the highest LDH content, i.e., LDH/rGO-10 and LDH/rGO-20 is two-fold higher than that reached by the calcined LDH of similar specific surface area.One can suggest that, due to the high dispersion of the LDH layers in the parent nanocomposites, both the number of coordinatively unsaturated O 2− sites at the edge of the mixed oxide platelets and their accessibility are enhanced after activation.When the CO 2 adsorption of nanocomposite materials is normalized per mass of LDH, it results in values significantly higher for all of them than for the bulk LDH, similarly to what has been reported for LDHs supported on CF [3], CNF [5,6] or MWCNT [27].
the mixed oxide platelets and their accessibility are enhanced after activation.When the CO2 adsorption of nanocomposite materials is normalized per mass of LDH, it results in values significantly higher for all of them than for the bulk LDH, similarly to what has been reported for LDHs supported on CF [3], CNF [5,6] or MWCNT [27].

Claisen-Schmidt Reaction
The Claisen-Schmidt condensation reaction between acetophenone and benzaldehyde in basic conditions can lead to different products: the chalcone isomers, i.e. trans-chalcone (1) and cischalcone (2), the Michael addition product (1,3,5-triphenylpentan-1-5-dione) (3) and the aldol addition product (4), as can be seen from Scheme 1.The generally accepted base-catalysed mechanism of Claisen-Schmidt condensation reaction starts with the abstraction of the acidic α-hydrogen of the ketone molecule by a base; the formed species undergoes a keto-enol tautomerism.The rate determining step of the entire reaction is the nucleophilic addition of the enolate, the anion of acetophenone, to the carbonyl carbon of the benzaldehyde, yielding the intermediate β-hydroxyl ketone, followed by dehydration to give chalcone (Scheme 2).The solvent where a chemical reaction takes place is rarely a non-inert medium.Its complex interactions with solute molecules and possible intermediates can result in a modification of the reaction pathway.In our study we have chosen three different solvents, i.e. polar methanol (MeOH), polar aprotic acetonitrile (ACN) and non-polar toluene whose physical constants are depicted in Table 3.The different products yields can allow more finely defining the influence of the textural properties and the basicity of the catalysts, particularly when one considers that formation of Michael addition product accounts for the presence of strong basic sites and/or for diffusional limitations favouring consecutive reactions.The production of Michael addition product also enhances with the temperature [15,28].
The reaction carried out at 40 • C in the different solvents and in absence of solvent with the activated LDH/rGO nanocatalysts allows reaching 100% conversion after 4 h in all cases while the conversion with the calcined LDH reaches values rather close to 100% after 8 h.Such differences of activity between the LDH/rGO nanocatalysts and the calcined LDH are in agreement with those previously reported for the acetone self-condensation [10].For the chalcone synthesis Climent et al. reported conversions of 4% and 82% after 1 h at 50 • C without solvent with the calcined and the calcined-rehydrated LDH sample, respectively, while Lopez et al. reported conversions of 4.6% and 70%, respectively, with the same type of catalysts after 3 h at 150 • C in DMF [15,18].Although the reaction was performed in different conditions (temperature, catalyst/reactants mass ratio, reaction time), it is noteworthy that the LDH/rGO nanocomposites and the calcined-rehydrated LDHs are both more active than the calcined LDH, i.e. the Mg(Al)O mixed oxide.In the case of rehydrated LDHs, this enhancement in activity has been attributed to the presence of intercalated OH − anions acting as Brönsted basic sites known to be the most active in aldol-type reactions.These reactions are indeed usually performed with NaOH or KOH in homogeneous catalysis.In our case, the increase in activity with the LDH/rGO nanocomposites respect to the calcined LDH likely accounts for an increase of the number and availability of the Lewis-type basic sites.rGO and LDH/rGO-0.5, the nanocomposite containing the lower amount of LDH, were not active in the condensation reaction of acetophenone and benzaldehyde, in accordance with the behaviour previously reported for acetone self-condensation reaction [10].Thus, in the following we will only consider the results from the nanocomposites with LDH:rGO ≥ 1.
The selectivities obtained after 8 h with the bare LDH calcined at 450 • C reveal the influence of the presence of solvent and of its nature (Table 4).Without solvent trans-chalcone (1) and Michael addition product (3) were obtained accounting for the presence in the catalyst of strong basic sites able to achieve the consecutive reaction between acetophenone and chalcone.The differences of selectivities observed with ACN and methanol cannot be related to their dielectric constant and are more likely related to their respective acidities.ACN of weak acidity poisons the stronger basic sites thus slightly decreasing the formation of the Michael addition product in comparison to the reaction without solvent.Moreover, as ACN is a polar aprotic solvent, hydrogen bonds with the anionic adducts, i.e. the enolate anion, are hindered during the reaction.The interaction between the non-solvated anion and the surface of the catalysts is thus favoured and consequently improves the formation of chalcone.
Methanol, a polar solvent of higher acidity than ACN, also poisons the basic sites of medium strength.The formation of aldol (4) as only side-product suggests that the dehydration step of the Claisen-Schmidt condensation is inhibited.This reaction proceeds by an E1cB mechanism (Scheme 3), in two steps.In the first step the basic site abstracts a proton from the α-C resulting in a carbanion which, in the second step, forms a π-bond and push the leaving group producing chalcone.This E1cB mechanism is strongly favored in presence of a strong base, but the use of a slightly acidic solvent might poison the basic centers.Likewise, the anion formed in the first step of reaction (see Scheme 3) may abstract a proton from MeOH thus inhibiting the reactivity towards the elimination step.Therefore, the selectivity towards chalcone decreases and that towards aldol product increases as the poisoning of the basic sites by methanol increases.Consequently, chalcone is produced in lower yield than with ACN and at the expense of the aldol product (4), while formation of the Michael addition product (3) is totally inhibited.
Toluene behaves similarly to ACN leading to chalcone (1 and 2) and Michael addition product (3).This accounts also for its very weak acidity and, probably, for differences of adsorption of the reactants with this non polar solvent.
A similar general behaviour is observed with the LDH/rGO catalysts than with the calcined LDH with differences depending on the composition of the nanocomposites (Tables 5-7).Chalcone is the main product observed without solvent as well as with ACN and toluene as solvents.The higher selectivity towards chalcone and particularly trans-chalcone (1) is obtained with ACN (Figure 6A and Table 5).It is noticeable that the selectivity towards cisand trans-chalcone ((1) + ( 2)) increases from 83 to 100% at the expense to that of the Michael addition product (3) which decreases from 17 to 8% when going from LDH/rGO-1 to LDH/rGO-5.This by-product is not formed with LDH/rGO-10 and LDH/rGO-20 as catalysts.This suggests the presence of a larger amount of stronger basic sites poisoned by ACN in these latter samples thus inhibiting the consecutive condensation of acetophenone and chalcone.LDH-rGO-20 and LDH-rGO-10 lead to the higher yields of trans-chalcone (1) and cis-chalcone (2), respectively and, most importantly, are totally selective for the formation of chalcone isomers.However, LDH-rGO-10 with a cis-chalcone (2) yield of 20% exhibits a peculiar behaviour among the series of catalysts.No aldol product (4) was obtained with ACN as solvent, no matter the composition of the nanocatalysts.It is also remarkable that the LDH/rGO nanocatalysts exhibit higher activity and selectivity towards transand cis-chalcone (1, 2) than the calcined LDH (Table 5).Since this latter is the catalytically active phase in the nanocomposites, this proves the synergistic effect produced by the hybridization of LDH and rGO.This synergistic effect is assigned to the smaller size and the higher dispersion of the LDH crystallites on the rGO surface as showed by TEM.
with differences depending on the composition of the nanocomposites (Tables 5-7).Chalcone is the main product observed without solvent as well as with ACN and toluene as solvents.
The higher selectivity towards chalcone and particularly trans-chalcone (1) is obtained with ACN (Figure 6A and Table 5).It is noticeable that the selectivity towards cis-and trans-chalcone ((1) + ( 2)) increases from 83 to 100% at the expense to that of the Michael addition product (3) which decreases from 17 to 8% when going from LDH/rGO-1 to LDH/rGO-5.This by-product is not formed with LDH/rGO-10 and LDH/rGO-20 as catalysts.This suggests the presence of a larger amount of stronger basic sites poisoned by ACN in these latter samples thus inhibiting the consecutive condensation of acetophenone and chalcone.LDH-rGO-20 and LDH-rGO-10 lead to the higher yields of trans-chalcone (1) and cis-chalcone (2), respectively and, most importantly, are totally selective for the formation of chalcone isomers.However, LDH-rGO-10 with a cis-chalcone (2) yield of 20% exhibits a peculiar behaviour among the series of catalysts.No aldol product (4) was obtained with ACN as solvent, no matter the composition of the nanocatalysts.It is also remarkable that the LDH/rGO nanocatalysts exhibit higher activity and selectivity towards trans-and cis-chalcone (1,2) than the calcined LDH (Table 5).Since this latter is the catalytically active phase in the nanocomposites, this proves the synergistic effect produced by the hybridization of LDH and rGO.This synergistic effect is assigned to the smaller size and the higher dispersion of the LDH crystallites on the rGO surface as showed by TEM.When methanol is used as solvent cis-chalcone (2), trans-chalcone (1) and aldol (4) are only obtained while the Michael addition does not occur (Figure 6B and Table 6).There is a general trend towards a decrease of the chalcone yield ((1) + ( 2)) at the expense of the aldol yield (4) as the LDH content in the LDH/rGO nanocatalysts increases, except for LDH/rGO-10 again exhibiting a peculiar When methanol is used as solvent cis-chalcone (2), trans-chalcone (1) and aldol (4) are only obtained while the Michael addition does not occur (Figure 6B and Table 6).There is a general trend towards a decrease of the chalcone yield ((1) + ( 2)) at the expense of the aldol yield (4) as the LDH content in the LDH/rGO nanocatalysts increases, except for LDH/rGO-10 again exhibiting a peculiar behaviour as already noted with ACN as solvent (Table 6 and Figure 6B).Moreover, the 1,4 addition of acetophenone on chalcone leading to the Michael addition product (3) is inhibited.LDH/rGO-1 and LDH/rGO-2 lead to the higher chalcone yields and exhibit similar behaviour than the calcined LDH in agreement with their closer basic properties.

Catalyst Yield of 1 (%) Yield of 2 (%) Yield of 3 (%)
Yield of 4 (%) behaviour as already noted with ACN as solvent (Table 6 and Figure 6B).Moreover, the 1,4 addition of acetophenone on chalcone leading to the Michael addition product (3) is inhibited.LDH/rGO-1 and LDH/rGO-2 lead to the higher chalcone yields and exhibit similar behaviour than the calcined LDH in agreement with their closer basic properties.When toluene is used as solvent, trans-chalcone (1), cis-chalcone (2) and Michael addition product (3) were formed (Figure 6C and Table 7).A remarkable feature is that toluene gives rise to the higher cis-chalcone and Michael addition product yields among all the solvents studied, despite cis-chalcone being less thermodynamically stable than trans-chalcone due to the strong steric effects between the carbonyl group and the aryl ring.Our catalytic results show that different chalcone isomer ratios are observed accounting for modifications of the interaction among reactants and the solvent, and depending on the composition of the catalysts whose polarity is related to the LDH:rGO weight ratio.Aromatic rings interact with the surface of rGO by competitive π-π interactions.In the cases of ACN and methanol as solvents, the π-π interaction between the reactants and the surface of the catalyst more likely occurs via a parallel orientation of the aromatic rings to the surface, thus favouring the formation of transchalcone.In the case of toluene as solvent, the interaction with both the surface of catalyst and the reactants is favoured due to their similar geometry and polarity.Moreover, reactants solvated by toluene are in less close proximity to the surface.This allows a T-shape π-π interaction between aromatic rings of reactants and the surface of the catalyst increasing the formation of cis-chalcone (Scheme 4).
behaviour as already noted with ACN as solvent (Table 6 and Figure 6B).Moreover, the 1,4 addition 404 of acetophenone on chalcone leading to the Michael addition product (3) is inhibited.LDH/rGO-1

405
and LDH/rGO-2 lead to the higher chalcone yields and exhibit similar behaviour than the calcined

406
LDH in agreement with their closer basic properties. 407

427
behaviour as already noted with ACN as solvent (Table 6 and Figure 6B).Moreover, the 1,4 addition 404 of acetophenone on chalcone leading to the Michael addition product (3) is inhibited.LDH/rGO-1

405
and LDH/rGO-2 lead to the higher chalcone yields and exhibit similar behaviour than the calcined

406
LDH in agreement with their closer basic properties. 407

420
the π-π interaction between the reactants and the surface of the catalyst more likely occurs via a 421 parallel orientation of the aromatic rings to the surface, thus favouring the formation of trans-behaviour as already noted with ACN as solvent (Table 6 and Figure 6B).Moreover, the 1,4 addition of acetophenone on chalcone leading to the Michael addition product (3) is inhibited.LDH/rGO-1 and LDH/rGO-2 lead to the higher chalcone yields and exhibit similar behaviour than the calcined LDH in agreement with their closer basic properties.When toluene is used as solvent, trans-chalcone (1), cis-chalcone (2) and Michael addition product (3) were formed (Figure 6C and Table 7).A remarkable feature is that toluene gives rise to the higher cis-chalcone and Michael addition product yields among all the solvents studied, despite cis-chalcone being less thermodynamically stable than trans-chalcone due to the strong steric effects between the carbonyl group and the aryl ring.Our catalytic results show that different chalcone isomer ratios are observed accounting for modifications of the interaction among reactants and the solvent, and depending on the composition of the catalysts whose polarity is related to the LDH:rGO weight ratio.Aromatic rings interact with the surface of rGO by competitive π-π interactions.In the cases of ACN and methanol as solvents, the π-π interaction between the reactants and the surface of the catalyst more likely occurs via a parallel orientation of the aromatic rings to the surface, thus favouring the formation of transchalcone.In the case of toluene as solvent, the interaction with both the surface of catalyst and the reactants is favoured due to their similar geometry and polarity.Moreover, reactants solvated by toluene are in less close proximity to the surface.This allows a T-shape π-π interaction between aromatic rings of reactants and the surface of the catalyst increasing the formation of cis-chalcone (Scheme 4).When toluene is used as solvent, trans-chalcone (1), cis-chalcone (2) and Michael addition product (3) were formed (Figure 6C and Table 7).A remarkable feature is that toluene gives rise to the higher cis-chalcone and Michael addition product yields among all the solvents studied, despite cis-chalcone being less thermodynamically stable than trans-chalcone due to the strong steric effects between the carbonyl group and the aryl ring. of acetophenone on chalcone leading to the Michael addition product (3) is inhibited.LDH/rGO-1 and LDH/rGO-2 lead to the higher chalcone yields and exhibit similar behaviour than the calcined LDH in agreement with their closer basic properties.When toluene is used as solvent, trans-chalcone (1), cis-chalcone (2) and Michael addition product (3) were formed (Figure 6C and Table 7).A remarkable feature is that toluene gives rise to the higher cis-chalcone and Michael addition product yields among all the solvents studied, despite cis-chalcone being less thermodynamically stable than trans-chalcone due to the strong steric effects between the carbonyl group and the aryl ring.Our catalytic results show that different chalcone isomer ratios are observed accounting for modifications of the interaction among reactants and the solvent, and depending on the composition of the catalysts whose polarity is related to the LDH:rGO weight ratio.Aromatic rings interact with the surface of rGO by competitive π-π interactions.In the cases of ACN and methanol as solvents, the π-π interaction between the reactants and the surface of the catalyst more likely occurs via a parallel orientation of the aromatic rings to the surface, thus favouring the formation of transchalcone.In the case of toluene as solvent, the interaction with both the surface of catalyst and the reactants is favoured due to their similar geometry and polarity.Moreover, reactants solvated by toluene are in less close proximity to the surface.This allows a T-shape π-π interaction between aromatic rings of reactants and the surface of the catalyst increasing the formation of cis-chalcone (Scheme 4).
of acetophenone on chalcone leading to the Michael addition product (3) is inhibited.LDH/rGO-1

405
and LDH/rGO-2 lead to the higher chalcone yields and exhibit similar behaviour than the calcined

406
LDH in agreement with their closer basic properties.
407  407   When toluene is used as solvent, trans-chalcone (1), cis-chalcone (2) and Michael addition product (3) were formed (Figure 6C and Table 7).A remarkable feature is that toluene gives rise to the higher cis-chalcone and Michael addition product yields among all the solvents studied, despite cis-chalcone being less thermodynamically stable than trans-chalcone due to the strong steric effects between the carbonyl group and the aryl ring.Our catalytic results show that different chalcone isomer ratios are observed accounting for modifications of the interaction among reactants and the solvent, and depending on the composition of the catalysts whose polarity is related to the LDH:rGO weight ratio.Aromatic rings interact with the surface of rGO by competitive π-π interactions.In the cases of ACN and methanol as solvents, the π-π interaction between the reactants and the surface of the catalyst more likely occurs via a parallel orientation of the aromatic rings to the surface, thus favouring the formation of transchalcone.In the case of toluene as solvent, the interaction with both the surface of catalyst and the reactants is favoured due to their similar geometry and polarity.Moreover, reactants solvated by toluene are in less close proximity to the surface.This allows a T-shape π-π interaction between aromatic rings of reactants and the surface of the catalyst increasing the formation of cis-chalcone (Scheme 4).Our catalytic results show that different chalcone isomer ratios are observed accounting for modifications of the interaction among reactants and the solvent, and depending on the composition of the catalysts whose polarity is related to the LDH:rGO weight ratio.Aromatic rings interact with the surface of rGO by competitive π-π interactions.In the cases of ACN and methanol as solvents, the π-π interaction between the reactants and the surface of the catalyst more likely occurs via a parallel orientation of the aromatic rings to the surface, thus favouring the formation of trans-chalcone.In the case of toluene as solvent, the interaction with both the surface of catalyst and the reactants is favoured due to their similar geometry and polarity.Moreover, reactants solvated by toluene are in less close proximity to the surface.This allows a T-shape π-π interaction between aromatic rings of reactants and the surface of the catalyst increasing the formation of cis-chalcone (Scheme 4).Cleaner synthetic routes, easier to handle, involving few or absence of solvent are currently desired in order to develop "green" processes.For this purpose and also to more finely define the LDH/rGO nanocatalysts interaction with the reagents, a series of experiments were conducted without solvent (Figure 6D and Table 8).Chalcone, with a larger selectivity towards trans-chalcone  It must be noted that higher Michael addition product yield is obtained without solvent than with ACN and toluene confirming the poisoning effect of these weakly acidic solvents on the strong basic sites.As expected, the Michael addition product yield also increases with the LDH content in the nanocomposites according to their increasing basicity.It reaches a maximum for the LDH/rGO-10 catalyst, which confirms its different behaviour compared to the other samples in the series.The increase of LDH content also decreased the selectivity towards the cis-chalcone, demonstrating that the presence of this product (thermodynamically unfavoured compared to trans-chalcone) in all the other experiments might be influenced by the presence of the solvent, which can act as stabilizer, especially in the case of toluene.It must be noted that higher Michael addition product yield is obtained without solvent than with ACN and toluene confirming the poisoning effect of these weakly acidic solvents on the strong basic sites.As expected, the Michael addition product yield also increases with the LDH content in the nanocomposites according to their increasing basicity.It reaches a maximum for the LDH/rGO-10 catalyst, which confirms its different behaviour compared to the other samples in the series.The increase of LDH content also decreased the selectivity towards the cis-chalcone, demonstrating that the presence of this product (thermodynamically unfavoured compared to trans-chalcone) in all the other experiments might be influenced by the presence of the solvent, which can act as stabilizer, especially in the case of toluene.
The results above reported show that the LDH/rGO nanocomposites are efficient base catalysts for the Claisen-Schmidt condensation reaction between acetophenone and benzaldehyde.Due to the strong basicity of the catalysts, consecutive reaction leading to the Michael addition product occurs when the reaction is performed without solvent.However, performing the reaction in a slightly acidic solvent such as ACN allows obtaining total selectivity towards chalcone with the most basic LDH/rGO-10 and LDH/rGO-20 catalysts.The LDH/rGO nanocatalysts are by far more active than the calcined LDH, and total conversion is obtained after 4 h at 40 • C (against 8 h for bare LDH).This shows that the dispersion of the active Mg(Al)O mixed oxide phase in the activated nanocomposites creates strong and accessible O 2− basic sites which results in improved Lewis basicity compared to bare calcined LDH.The Brønsted-type basic sites in the calcined-rehydrated LDHs yet exhibit better efficiency than the Lewis-type basic sites in the LDH/rGO nanocomposites as reported in previous studies [15,18].However, since the superior activity of the LDH/rGO catalysts with respect to bare calcined LDH has been proved, LDH/rGO materials are expected to boost their activity after proper rehydration/reconstruction.It must be point out that the objective of this work was to demonstrate that calcined LDH/rGO hybrids have fine properties which make them active heterogeneous base catalysts in different reactions of interest.The nature of sites was not investigated.So, catalysis with rehydrated hybrids was not included in this manuscript.The rehydration procedure (i.e.gas or liquid phase), time, temperature and even drying mode are parameters known to strongly affect the final catalyst properties.Furthermore, rehydration depends on the characteristics of the hybrid itself (i.e.loading of LDH, type of preparation and drying...) and could be kinetically limited.So that efforts are still needed to make a protocol that allows obtaining rehydrated samples accurately and in a reproducible way.

Summary and Conclusions
Here, it has been demonstrated that LDH/rGO nanomaterials present Lewis-type basic properties which are highly tunable.TEM analysis revealed the intimate contact between the LDH and graphene components in all the cases.The basic properties of the thermally activated LDH/rGO materials were evaluated by CO 2 adsorption, finding that the number of sites, was dependant on the LDH:rGO mass ratio.The physico-chemical properties of the LDH/rGO samples of different compositions were mirrored on their catalytic activity higher than that showed by bare LDH.Thus, total conversion at 40 • C was obtained after 4 h and 8h over LDH/rGO nanocatalysts and bare LDH, respectively.The superior activity of the LDH/rGO nanocatalysts accounts for the great dispersion of the active Mg(Al)O mixed oxide nanoplatelets, which creates strong and accessible O 2− basic sites, especially at higher amount of LDH, i.e., for LDH/rGO-10 and LDH/rGO-20.Remarkably, these two catalysts presented total selectivity towards the chalcone isomers in appropriate conditions, since the solvent plays an important role on the products distribution.
The specific behaviour of LDH/rGO nanocatalysts was observed when the reaction was performed in absence of solvent, where high yields of Michael addition product (3) were observed, especially with LDH/rGO-10 and LDH/rGO-20.This clearly indicates that basic sites present in the nanocomposite catalysts favour the subsequent condensation via 1,4-addition of acetophenone on chalcone in contrast to the rehydrated LDHs [14,17].This further highlights the high strength of the Lewis-type basic sites generated by hybridization of LDH and rGO required for the Michael addition.On the contrary, the weak-medium strength of the Brønsted-type basic sites in the rehydrated LDHs cannot undergo 1,4-addition of acetophenone to chalcone.
Lopez et al. and Climent et al. [15,18] have reported higher activity for calcined/rehydrated LDH at 150 • C than LDH/rGO catalysts.However, the later present advantages such as high catalytic activity and selectivity towards chalcone under very soft liquid phase conditions (40 • C).Besides, LDH/rGO materials are expected to boost their activity after proper rehydration/reconstruction.
The high activity of LDH/rGO nanocatalysts, in combination with their high tunability through their composition, makes these materials promising candidates as solid base catalysts, opening a path to new applications of graphene-based nanocomposites which should be further studied.

Figure 2 .
Figure 2. N2 adsorption-desorption isotherms of: (A) as-synthesized LDH and LDH/rGO materials and (B) LDH and LDH/rGO materials after treatment at 450 °C under Ar for 5 h.(Isotherms are displaced along ordinate axis to a better lecture).

Figure 2 .
Figure 2. N 2 adsorption-desorption isotherms of: (A) as-synthesized LDH and LDH/rGO materials and (B) LDH and LDH/rGO materials after treatment at 450 • C under Ar for 5 h.(Isotherms are displaced along ordinate axis to a better lecture).

ChemEngineering 2019 ,
3, x FOR PEER REVIEW 7 of 17 observed suggest, on the contrary, the formation of homogeneous structure in materials with LDH:rGO ≥ 1.Therefore, as the LDH content increases, dispersion of the LDH platelets on the rGO surface may be improved and/or the GO restacking is reduced by the alternative LDH/GO stacking interactions as previously suggested [10,23].The specific surface area decreases to 25 m 2 •g −1 at low LDH content for the LDH/rGO-0.5composite, well below the specific surface area of the bare LDH, accounting for high aggregation of the LDH particles which, in addition, do not hinder the restacking of the GO layers.

Figure 5 .
Figure 5. HRTEM of sample LDH/rGO-10 (A) showing the good dispersion and contact between components and (B) detailed structural HRTEM analisyis.

286Figure 5 .
Figure 5. HRTEM of sample LDH/rGO-10 (A) showing the good dispersion and contact between components and (B) detailed structural HRTEM analisyis.After calcination at 450 • C, the values of the specific surface areas increase up to 1.4 and 2.2 times at low (LDH/rGO-1) and high (LDH/rGO-20) LDH content, respectively, in comparison to the non-calcined nanocomposites.This is in agreement with the structural transformation of the Mg-Al LDH component into Mg(Al)O mixed oxide of higher surface area as confirmed with the bare LDH whose specific surface area increases from 140 to 280 m 2 •g −1 .This suggests that the steadiness of the surface area in non-calcined hybrids may be related (in different extent) to both intrinsic porosity generated by incorporation of LDH in the hybrids as well as interporosity due to the lower stacking degree of both components (i.e., rGO and LDH) forming the nanocomposite.Whereas, the increase in surface area in calcined materials is due to the pore generation produced by gas release during the LDH decomposition upon thermal treatment confirmed by XRD (Figure1).Volumetric adsorption of CO 2 at low pressure was applied to determine the number of basic sites on the LDH/rGO nanocomposites activated by in situ calcination at 450 • C. The amount of CO 2 adsorbed and then the number of basic sites significantly increases from 52 to 265 µmol•g −1 with the LDH content in the nanocomposites (Table2).This is in accordance with earlier studies on basicity characterization of LDH/rGO nanocomposites[10,23,26].In the analysis conditions of our experiments, the CO 2 adsorption capacity of the bare rGO was found negligible.It is notable that CO 2 adsorption capacity of sample LDH/rGO-0.5 was around two times lower than that reached by the activated bare LDH and LDH/rGO-1 samples.This is consistent with the morphology and texture of LDH/rGO-0.5 giving rise to low accessibility of the probe to the basic sites.On the other hand, the CO 2 adsorption capacity of the samples having the highest LDH content, i.e., LDH/rGO-10 and LDH/rGO-20 is two-fold higher than that reached by the calcined LDH of similar specific surface area.One can suggest that, due to the high dispersion of the LDH layers in the parent nanocomposites, both the number of coordinatively unsaturated O 2− sites at the edge of the

Table 4 .Table 5 .*
Product yields with bulk LDH after 8 h of reaction at 40 • C in the different solvents media.Solvent Yield of 1 (%) Yield of 2 (%) Yield of 3 (%) Yield of 4 (%) elimination step.Therefore, the selectivity towards chalcone decreases and that towards aldol product increases as the poisoning of the basic sites by methanol increases.Consequently, chalcone is produced in lower yield than with ACN and at the expense of the aldol product (4), while formation of the Michael addition product (3) is totally inhibited.Product yields after 4 h of reaction in aprotic acetonitrile (ACN) at 40 °C for all activated catalysts.Catalyst Yield of 1 (%) Yield of 2(%) Yield of 3 (%) Yield of 4 (After 8 h of reaction ChemEngineering 2019, 3, x FOR PEER REVIEW 11 of 17 solvated anion and the surface of the catalysts is thus favoured and consequently improves the formation of chalcone.

Table 5 .
Scheme 3. The E1cB mechanism involved in the chalcone formation.

Table 5 .
Product yields after 4 h of reaction in aprotic acetonitrile (ACN) at 40 • C for all activated catalysts.Catalyst Yield of 1 (%) Yield of 2 (%) Yield of 3 (%) Yield of 4 (%) solvated anion and the surface of the catalysts is thus favoured and consequently improves the formation of chalcone.

Table 4 .
Scheme 3. The E1cB mechanism involved in the chalcone formation.

Table 4 .
Scheme 3. The E1cB mechanism involved in the chalcone formation.

409Table 7 .416
When toluene is used as solvent, trans-chalcone(1), cis-chalcone(2) and Michael addition 410 product (3) were formed (Figure6Cand Table7).A remarkable feature is that toluene gives rise to 411 the higher cis-chalcone and Michael addition product yields among all the solvents studied, despite 412 cis-chalcone being less thermodynamically stable than trans-chalcone due to the strong steric effects 413 between the carbonyl group and the aryl ring.414Product yields after 4 h of reaction in toluene at 40 °C for all activated catalysts.Our catalytic results show that different chalcone isomer ratios are observed accounting for 417 modifications of the interaction among reactants and the solvent, and depending on the composition 418 of the catalysts whose polarity is related to the LDH:rGO weight ratio.Aromatic rings interact with 419 the surface of rGO by competitive π-π interactions.In the cases of ACN and methanol as solvents, 420 the π-π interaction between the reactants and the surface of the catalyst more likely occurs via a 421 parallel orientation of the aromatic rings to the surface, thus favouring the formation of trans-422 chalcone.In the case of toluene as solvent, the interaction with both the surface of catalyst and the 423 reactants is favoured due to their similar geometry and polarity.Moreover, reactants solvated by 424 toluene are in less close proximity to the surface.This allows a T-shape π-π interaction between 425 aromatic rings of reactants and the surface of the catalyst increasing the formation of cis-chalcone 426 (Scheme 4).

409Table 7 .416
When toluene is used as solvent, trans-chalcone(1), cis-chalcone(2) and Michael addition 410 product (3) were formed (Figure6Cand Table7).A remarkable feature is that toluene gives rise to 411 the higher cis-chalcone and Michael addition product yields among all the solvents studied, despite 412 cis-chalcone being less thermodynamically stable than trans-chalcone due to the strong steric effects 413 between the carbonyl group and the aryl ring.414Product yields after 4 h of reaction in toluene at 40 °C for all activated catalysts.Our catalytic results show that different chalcone isomer ratios are observed accounting for 417 modifications of the interaction among reactants and the solvent, and depending on the composition 418 of the catalysts whose polarity is related to the LDH:rGO weight ratio.Aromatic rings interact with 419 the surface of rGO by competitive π-π interactions.In the cases of ACN and methanol as solvents,

Table 7 .
Product yields after 4 h of reaction in toluene at 40 • C for all activated catalysts.
reaction and LDH/rGO-2 lead to the higher chalcone yields and exhibit similar behaviour than the calcined 406 LDH in agreement with their closer basic properties.
reaction of acetophenone on chalcone leading to the Michael addition product (3) is inhibited.LDH/rGO-1 and LDH/rGO-2 lead to the higher chalcone yields and exhibit similar behaviour than the calcined LDH in agreement with their closer basic properties.

440
It must be noted that higher Michael addition product yield is obtained without solvent than 441 with ACN and toluene confirming the poisoning effect of these weakly acidic solvents on the strong 442 basic sites.As expected, the Michael addition product yield also increases with the LDH content in

440
It must be noted that higher Michael addition product yield is obtained without solvent than 441 with ACN and toluene confirming the poisoning effect of these weakly acidic solvents on the strong 442 basic sites.As expected, the Michael addition product yield also increases with the LDH content in

Scheme 4 .
Scheme 4. π-π interaction among solvent, reactants and the surface of the catalyst.Up: parallel interaction between aromatic rings and rGO surface with non-aromatic solvents.Down: T-shape interaction favoured by toluene solvation.

( 1 )
is the main product of reaction.Michael addition product (3) is the only by-product formed according to the high basicity of the samples.Aldol (4) is formed in the case of LDH/rGO-1 due the lower basicity of this sample in the series of nanocomposites.

Table 2 .
Basicity results of the synthesized LDH and LDH/rGO nanocomposites.
a Referred to calcined material.

Table 2 .
Basicity results of the synthesized LDH and LDH/rGO nanocomposites.
a Referred to calcined material.

Table 3 .
Physical constants of the solvents studied in the Claisen-Schmidt condensation reaction.Scheme 2. Accepted mechanism of the Claisen-Schmidt condensation.

Table 3 .
Physical constants of the solvents studied in the Claisen-Schmidt condensation reaction.

Table 4 .
Product yields with bulk LDH after 8 h of reaction at 40 °C in the different solvents media.

Table 5 .
Product yields after 4 h of reaction in aprotic acetonitrile (ACN) at 40 °C for all activated catalysts.Catalyst Yield of 1 (%) Yield of 2(%) Yield of 3 (%) Yield of 4 (%) *After 8 h of reaction ChemEngineering 2019, 3, x FOR PEER REVIEW 11 of 17 solvated anion and the surface of the catalysts is thus favoured and consequently improves the 355 formation of chalcone.356

Table 4 .
Product yields with bulk LDH after 8 h of reaction at 40 °C in the different solvents media.

Table 6 .
Product yields after 4 h of reaction in methanol at 40 • C for all activated catalysts.

Table 6 .
Product yields after 4 h of reaction in methanol at 40 °C for all activated catalysts.

Table 7 .
Product yields after 4 h of reaction in toluene at 40 °C for all activated catalysts.

Table 6 .
Product yields after 4 h of reaction in methanol at 40 °C for all activated catalysts.

Table 6 .
Product yields after 4 h of reaction in methanol at 40 °C for all activated catalysts.

Table 6 .
Product yields after 4 h of reaction in methanol at 40 °C for all activated catalysts.

Table 7 .
Product yields after 4 h of reaction in toluene at 40 °C for all activated catalysts.

Table 6 .
Product yields after 4 h of reaction in methanol at 40 °C for all activated catalysts.
*After 8 h of reaction

Table 7 .
Product yields after 4 h of reaction in toluene at 40 °C for all activated catalysts.

Table 6 .
Product yields after 4 h of reaction in methanol at 40 °C for all activated catalysts.When toluene is used as solvent, trans-chalcone (1), cis-chalcone (2) and Michael addition 410 product (3) were formed (Figure6Cand Table7).A remarkable feature is that toluene gives rise to 411 the higher cis-chalcone and Michael addition product yields among all the solvents studied, despite 412 cis-chalcone being less thermodynamically stable than trans-chalcone due to the strong steric effects 413 between the carbonyl group and the aryl ring.

Table 7 .
Product yields after 4 h of reaction in toluene at 40 °C for all activated catalysts.

Table 6 .
Product yields after 4 h of reaction in methanol at 40 °C for all activated catalysts.When toluene is used as solvent, trans-chalcone (1), cis-chalcone (2) and Michael addition 410 product (3) were formed (Figure6Cand Table7).A remarkable feature is that toluene gives rise to 411 the higher cis-chalcone and Michael addition product yields among all the solvents studied, despite 412 cis-chalcone being less thermodynamically stable than trans-chalcone due to the strong steric effects 413 between the carbonyl group and the aryl ring.

Table 7 .
Product yields after 4 h of reaction in toluene at 40 °C for all activated catalysts.

Table 6 .
Product yields after 4 h of reaction in methanol at 40 °C for all activated catalysts.

Table 7 .
Product yields after 4 h of reaction in toluene at 40 °C for all activated catalysts.

Table 8 .
Product yields after 4 h of reaction without solvent at 40 °C for all activated catalysts.

Table 8 .
Product yields after 4 h of reaction without solvent at 40 °C for all activated catalysts.

Table 8 .
Product yields after 4 h of reaction without solvent at 40 °C for all activated catalysts.