Silicotungstic Acid Modified Bentonite : An Efficient Catalyst for Synthesis of Acetal Derivatives of Aldehydes and Ketones

Acetals and ketals are among the important materials of organic synthesis and as protecting agent of carbonyl functionality. A milder, efficient and green synthesis of acetals and ketals has been developed using Silicotungstic acid modified Bentonite (STA-Ben) as a catalyst. STA-Ben has been synthesized and characterized by various analytical techniques. It has been found to be an efficient and reusable catalyst for the synthesis of acetyl derivatives in excellent yields. In order to elucidate the efficiency of the STA-Ben as catalyst, reaction has also been performed using various catalysts. The reaction conditions (time and amount of catalyst) have been optimized using various catalysts. The products of the various reactions have been characterized by FT-IR, NMR.


Introduction
Acetals and ketals are one of the most important perfume materials and industrial materials of organic synthesis.The protection of carbonyl functionality as an acetal or thioacetal derivative is a common practice in organic synthesis owing to their stability under mild acidic and basic conditions.They are generally obtained by the condensation of carbonyl compound with acetic anhydride [1], diols, dithiols and orthoformates [2][3][4][5], using Lewis acids as catalysts.A variety of catalysts are employed for this purpose like CoCl 2 [6], NiCl 2 [2], HCl [7], HClO 4 [8], sulfated zirconia [9] etc.But the most recent methods employ MMT-K10 [10], ionic liquids [11], metal cation exchanged MMT [12], natural kaolinite clay [3], silica sulfuric acid [13], TaCl 5 -silicagel [14] as catalysts.However, many of these methods have some drawbacks such as low yields of the products, long reaction times, harsh reaction conditions, difficulties in workup.Moreover, the main disadvantage of almost all existing methods is that the catalysts are destroyed in the work-up procedure and cannot be recovered or reused.Therefore, there is further scope to explore mild and efficient methods for acetalization of carbonyl compounds.
Solid acids offer many advantages by their nature, over soluble counterparts such as aluminium chloride and hydrogen fluoride.The substitution of liquid acids by solids as catalysts for organic synthesis offers a potential for superior effectiveness and environmental integrity.Although they differ in structure from liquid acids, solid acid catalysts work by the same principle.Among the solid acids, heteropoly acids (HPAs) have been extensively studied as acid catalysts for many reactions and found industrial applications in several processes [15].The Keg-gin-type HPAs typically represented by the formula H 8−x [XM 12 O 40 ], where X is the heteroatom (e.g., P 5+ or Si 4+ ), x is its oxidation state and M is the addenda atom (usually Mo 6+ or W 6+ ), are the most important catalysts, especially H 3 PW 12 O 40 (PW), H 3 PMo 12 O 40 (PMo) and H 4 SiW 12 O 40 (SiW) [16].They are more active than the conventional catalysts, such as mineral acids, ion-exchange resins, zeolites, SiO 2 /Al 2 O 3 and H 3 PO 4 /SiO 2 [17][18][19].
HPAs have several advantages over liquid acid catalysts, including being non-corrosive and environmen-tally benign.Thus, they present fewer disposal problems and more economically and environmentally attractive.Heteropoly acids (HPAs) due to their strong acidity have attracted much interest as the catalysts mostly in homogeneous systems [20,22].It's not easy to separate HPA from reaction mixture and reuse it unless it is supported on some catalyst.Clays have also been proposed as suitable acid catalysts [23,24].Clays are furthermore used as adsorbents, decoloration agents, ion exchangers, and catalysts [25].The use of clays, as heterogeneous catalysts, offers many advantages over homogeneous acid catalysts such as ease of separation, mild reaction conditions, better selectivity of the desired product, and elimination of waste disposal problems.In a large number of organic reactions clays have been used as catalysts on laboratory/ industrial scales.The properties of clay can further be improved by making pillared clays.Pillared clays are clays with high permanent porosity obtained by separating the clay sheets by a molecular prop or pillaring agent.These pillaring agents can be organic, organometallic, or inorganic complexes, preferably of a high positive charge.Pillared clay (PILC) possesses several interesting properties, such as large surface area, high pore volume and tunable pore size (from micropore to mesopore), high thermal stability, strong surface acidity and catalytic active substrates/metal oxide pillars.These unique characteristics make PILC an attractive material in catalytic reactions.It can be made either as catalyst support or directly used as catalyst [26][27][28].
In the present work silicotungstic acid (a heteropoly acid) modified bentonite have been synthesized to explore the properties of both clay and silicotungstic acid (a heteropoly acid).This makes it possible to carry out the catalytic process at a lower catalyst concentration and/or at a lower temperature.Further, catalysis of heteropoly acid lacks side reactions.

Catalyst Preparation
Na-Bentonite 1.0 g of Bentonite clay was added into a 250 ml conical flask containing 50 ml of 1.0 M NaCl this clay suspension was stirred for 16 hours.The residue after centrifugation was washed several times with double distilled water till complete removal of chloride ions.The residue thus obtained after above procedure was dried in an oven at 100˚C to generate the Na form of the Bentonite (Na-Ben).

Al-Pillared Bentonite (Al-Ben)
In a 250 ml conical flask containing 1.0 g of Na-Ben in 100 ml of double distilled water, 50 ml of the pillaring solution (keggin ion) was gradually added with vigorous stirring for 16 hours.The residue was washed several times with double distilled water till the complete removal of chloride ions was confirmed by AgNO 3 test.The residue, thus obtained was dried in an oven at 100˚C is referred to as Al-Pillared Bentonite (Al-Ben) [29,30].
Acid Activated Bentonite (H + -Ben) 5.0 g of Na-Ben was added into a 100 ml beaker containing 50 ml of 3N H 2 SO 4 , this mixture was exposed to microwave radiation for 30 minutes.The residue was washed several times with double distilled water till the complete removal of ions was confirmed by BaCl 2 test.The residue thus obtained was dried in an oven at 100˚C to generate the Acid activated Bentonite (H + -Ben) [28].Pillared Acid Activated Bentonite (PAA-Ben) 1.0 g of H + Ben, was added into a 250 ml conical flask containing 100 ml of double distilled water.50 ml of pillaring solution was gradually added with vigorous stirring for 16 hours.The residue was washed several times with double distilled water till the complete removal of chloride ions was confirmed by AgNO 3 test.The residue thus obtained was dried in an oven at 100˚C and is referred to as Pillared Acid Activated Bentonite (PAA-Ben).

Silicotungstic Acid Modified Bentonite (STA-Ben)
In a 250 ml conical flask, 1.0 g Na-Ben was suspended in 50 ml double distilled water.To this, aqueous solution of silicotungstic acid (100 mg) was added drop wise and then stirred for 16 hours.After this, the mixture was filtered and washed with double distilled water to remove the excess of silicotungstic acid.The product was dried at 100˚C.

General Procedure for the Synthesis of Acetal Derivative of Aldehydes and Ketones
In order to elucidate the role of the STA-Ben as catalyst, a controlled reaction was carried out using STA, bentonite, Al-Ben, H + -Ben, PAA-Ben and STA-Ben as catalyst with benzaldehyde as reactant.The best results were obtained with STA-Ben in microwave.
A number of aromatic/aliphatic aldehydes or ketones (10 mmol) and ethylene glycol (10 mmol) were mixed with the STA-Ben (50 mg).The mixture was exposed to microwave raditions.After irradiation of the mixture for a specified period, the contents were gradually cooled to room temperature.The completion of the reaction was checked by TLC.After confirming the completion of the reaction, the catalyst was recovered by filtration.The catalyst thus separated by filtration was washed 2 -3 times with absolute ethanol to remove organic matter.The residue obtained after evaporation of the solvent from the filtrate was purified using TLC/column chromatography with CHCl 3 :MeOH with increasing polarity.

Optimization of Reaction Conditions
For the optimization of reaction conditions 10 mmol of ethylene glycol and 10 mmol of Benzaldehyde have been selected as reactants.
Optimization of the Catalysts Amount Reactions have been performed using varying amount of different catalysts under uniform conditions (Table 1).

Optimization of Time
The reaction time has been optimized by performing reactions at regular intervals of time.After a certain time period there is not much increase in the yield.That time has been selected as optimum time (Table 2).
After optimization of time and amount of catalyst a number of acetal derivatives have been synthesized Table 3.

X-Ray Diffraction
The XRD pattern of Ben [33], Na-Ben and H + -Ben show a sharp peak at 2θ = 5.93, 6.83 and 9.67 respectively corresponding to a d-value of 14.9 Å, 12.9 Å and 9.1 Å.A decrease in the d-value of 2 Å and 5.8 Å is observed when interlayer cations (Ca 2+ ) are replaced by the    4. Total surface area of Ben has been found to be 215 m 2 /g.After conversion to Na-Ben total surface area has been found to be 121 m 2 /g which may be due to the decrease in d-spacing as indicated by XRD data.Total surface area of H + -Ben has been found to be 327 m 2 /g.Although Na ions are replaced by smaller H + ions, but acid activation also causes the formation of small pores, consequently increasing the surface area [34,35].Total surface area of Al-Ben has been found to be 295 m 2 /g.Due to the intercalation of Al-Keggin ion the inner surface also becomes assessable.PAA-Ben has been found to have a total surface area of 350 m 2 /g which is again due to intercalation of Al-Keggin ion in H + -Ben.Total surface area of STA-Ben has been found to be 298 m 2 /g which again shows intercalation of STA.

FT-IR
Vibrational spectra of Ben, Na-Ben, H + -Ben, Al-Ben and PAA-Ben (Figures 1 and 2) indicate two strong absorption bands ~3626 cm −1 and ~3436 cm −1 corresponding to the stretching vibrations of the O-H group originating from the surface adsorbed and interlayer water.The ~1642 cm −1 band in these samples has been assigned to the H-O-H bending vibrations of water.The ~1043 cm -1 and ~796 cm −1 bands are attributed to the stretching vibration of the Si-O bond.The ~522 cm −1 and ~466 cm −1 bands have been assigned to the Si-O-Al and Si-O-Si deformation vibrations respectively [31,32].The STA-Ben (Figure 3(b)) also shows the band in the similar region.The FT-IR spectra of STA (Figure 3(a)) shows an absorption band in the region of the ~3141 cm −1 and have been assigned to the stretching vibrations originating from the O-H groups present in the Keggin structure of STA.The absorption band at ~1711 cm −1 has been assigned to the bending vibrations of the O-H group.The

Thermal Method of Analysis
The thermogram (TGA) of Ben, Na-Ben, H + -Ben (Figure 4) shows four step weight loss pattern.The first step, up to 180˚C, corresponds to dehydration of surface adsorbed water.The second step, 180˚C to 550˚C, is attributed to dehydration of interlayer water.The third step 550˚C to 675˚C, is attributed to the gradual dehydroxylation of clay layers.Beyond 675˚C the clay loses its structure and practically shows no weight loss [31].
The thermogram (TGA) of PAA-Ben, Al-Ben (Figure 5) shows a similar four step weight loss pattern.The first step, up to 200˚C, corresponds to dehydration of surface adsorbed water.The second step, 200˚C to 350˚C, is attributed to dehydration of interlayer water.The third step, 350˚C to 600˚C, is attributed to the gradual dehydroxylation of clay layers.Beyond 600˚C the clay loses its structure and practically shows no weight loss [31].
The TGA of pure STA (Figure 6 weight losses.The first step, up to 300˚C, corresponds to the loss of water of crystallization.The second step, 300˚C to 500˚C, shows weight loss corresponding to the decomposition of keggin unit of STA [33]. The TGA of STA-Ben (Figure 6(b)) shows four step weight loss patterns, the first step, up to 150˚C, corresponds to dehydration of surface water.The second step, 150˚C to 350˚C, is attributed to dehydration of interlayer water.The third step, 350˚C to 750˚C, is attributed to the dehydroxylation of clay layers and the loss of keggin ion structure The heteropoly acids are stable up to 500˚C but after intercalation the catalyst becomes stable up to 750˚C.

SEM with EDX Analysis
The SEM-EDX pictures (magnification of 832X) of Ben and STA-Ben are represented in (Figures 7(a) and  (b)).The SEM pictures of Ben and STA-Ben show no distinct change in the surface morphology and appear to have the layered structure.Therefore, it appears that the STA is not adsorbed on the surface of the clay but is in the layers of the clay.This fact is also supported by the XRD and IR studies.The SEM results are also supported by the EDX analysis.In both the cases surface composition consist of Al, Si, O, Mg, Fe, Ca & K.No signal corresponding to W was supported by the EDX data which further shows that STA may be in the interlayers region.

Characterization of Acetal Derivatives
The acetal derivatives synthesized during the reaction has been characterized using FT-IR and NMR spectroscopy techniques.
1) Benzaldehyde acetal IR (υ in cm The thermal stability of the catalyst was found to be unaffected after reuse.(Figure 10).XRD and FTIR data (Figure 11) of STA-Ben has been found to have no significant change.

Conclusion
We have synthesized STA intercalated Bentonite which proved to be a highly efficient, reusable and environmental benign catalyst for synthesis of acetal derivatives of aldehydes and ketones.

3 #
Reactant is highly volatile.Therefore, the yield is very low.smaller ions, Na + and H + respectively.PAA-Ben, shows a further shift in the peak position, 2θ = 5.30 and a d-value of 16.6 Å corresponding to an increase in the interlayer region by 7.5 Å w.r.t H + -Ben confirms the intercalation of Al Keggin ion into the interlayer region of H + -Ben.The Al-Ben shows a peak at 2θ = 5.20 and a d-value of 16.9 Å corresponding to an increase in the d-value of 4 Å w.r.t Na-Ben thus confirming the intercalation of Al Keggin ion in the interlayer region of Na-Ben.STA-Ben, show a peak at 2θ = 5.47 corresponding to a d-value of Silicotungstic Acid Modified Bentonite: An Efficient Catalyst for Synthesis of Acetal Derivatives of Aldehydes and Ketones 196 16.1 Å.This increase in the d-value 3.2 Å w.r.t Na-Ben shows that STA is in the interlayer region of Na-Ben.Total Surface Area Total surface area studies have been performed by EGME method.Surface area values of Ben, Na-Ben, H + -Ben, Al-Ben, PAA-Ben, STA-Ben are represented in the Table