# Surface Modification of Fly Ash for Active Catalysis

Authors: Deepti Jain; Renu Hada; Ashu Rani
Journal: Journal of Catalysts
 (2013)

---

## Abstract

Fly ash based effective solid base catalyst (KF/Al2O3/fly ash473, KF/Al2O3/fly ash673, and KF/Al2O3/fly ash873) was synthesized by loading  KF over chemically and thermally activated fly ash. The chemical activation was done by treating fly ash with aluminum nitrate via precipitation method followed by thermal activation at 650°C to increase the alumina content in fly ash. The increased alumina content was confirmed by SEM-EDX analysis. The alumina enriched fly ash was then loaded with KF (10 wt%) and calcined at three different temperatures 473 K, 673 K and 873 K. The amount of loaded KF was monitored by XRD, FTIR spectroscopy, SEM-EDX, TEM and Flame Atomic Absorption Spectrophotometer. The catalytic activities of the catalysts were tested in the Claisen-Schmidt condensation of benzaldehyde and 4-methoxybenzaldehyde with 2′-hydroxyacetophenone to produce 2′-hydroxychalcone and 4-methoxy-2′-hydroxychalcone respectively. Higher conversion (83%) of benzaldehyde and (89%) of 4-methoxybenzaldehyde reveals that among these heterogeneous catalysts KF/Al2O3/fly ash673 is very active.


---

## Body

## 1. Introduction

Fluoride ion is useful as weakly basic, nonnucleophilic in many organic chemical processes involving hydrogen abstraction or hydrogen bond formation [1]. Fluoride has been reported as effective basic catalyst in Cannizzaro reaction to replace classical methods employing hydroxide base which gave large amount of Cannizzaro side reactions [2]. Potassium fluoride is a well-known source of fluoride and possesses a number of advantages of both solution and solid phase chemistry. Among the supported fluoride systems, potassium fluoride on activated alumina has been found to be more reactive than nonsupported KF, KF-silica gel, KF-celite and KF-molecular sieves [3]. When KF is loaded on alumina, it shows high catalytic activity towards organic reactions namely. Michael addition [4], aldol condensation [5] and transesterification reactions [6].  The basic sites on KF/alumina may be related to a very hard anion F−; the catalyst may show the characteristic performances which differentiate KF/alumina from the oxide-type solid base catalysts such as alkaline earth oxides [7]. In contrast  to  many  applications  of  KF/alumina  to  organic  synthesis  as  a  base  catalyst, mechanisms of the appearance of  the basicity of KF/alumina are not clarified. Insufficient coordination of KF only with surface OH groups may result in the formation of active F− ions [8]. This possibility was supported by 19F MAS NMR [9]. Three basic species or mechanisms of the appearance of the basicity of KF/alumina reported previously [10] are (a) the presence of active fluoride, (b) the presence of [Al–O–] ion which generates OH−  when water is added, and  (c)  the  cooperation  of  F−   and  [Al–OH].  It  has  been  reported  in the literature (1)  that  the formation  of  potassium  hexafluoroaluminate  must  be  accompanied  by  the  formation  of hydroxide and/or aluminate, responsible for the high reactivity of KF/Al2O3. However, F− ion has little or no direct role in the catalytic activity of KF/Al2O3 catalyst:
(1)12KF+Al2O3+3H2O⟶2K3AlF6+6KOH
The strong basic nature of KF/Al2O3   allowed it to replace organic bases in a number of organic reactions.The Claisen-Schmidt condensation between acetophenone and benzaldehyde derivatives is a valuable C–C bond-forming reaction which producesα,β-unsaturated ketones called chalcones which display a wide spectrum of biological activities including  antioxidant, antibacterial, antileishmanial, anticancer, antiangiogenic, anti-infective and anti-inflammatory activities  [11–13].  Traditionally, the Claisen-Schmidt condensation is carried out, using alkaline hydroxides or sodium ethoxide [14]. The use of basic solids, such as zeolites [15], alkali  metal  and  oxides  supported  on  alkaline  earth  oxide  [16],   MgO  [17], calcined hydrotalcites [18] and KF [19], has received much attention over the last years as potential catalysts for Claisen-Schmidt condensations. Using solid catalysts, instead of stoichiometric amounts  of  soluble  strong  bases,  the  overall  atom  efficiency  of  reactions  is  improved, processes are simplified,  the  turn overnumber of the catalyst is increased, the volume of waste is significantly reduced, and product  workup becomes easier, if necessary at all. Typically organic bases immobilized on different  supports have been  used as catalytic materials. Progress has predominately been limited because of leaching of the active material from the various types of support used.Fly ash (SiO2, Al2O3, Fe2O3, CaO, and MgO) by appropriate activation has been converted into solid acids and solid bases. H2SO4  treated fly ash has been used as Bronsted acid catalyst for synthesis of aspirin and oil of wintergreen as solid support for loading of cerium triflate and sulphated zirconia [20–22] for synthesis of 3,4-dimethoxyacetophenone (antineoplastic) and diphenylmethane. In recent years, fly ash treated with CaO, NaOH, MgO and aminopropyl trimethoxysilane has also been used as solid base catalysts in various condensation reactions [23–26]. In the present work, we attempted to introduce a novel solid base catalyst from chemically activated fly ash by loading KF followed by thermal activation at different temperatures. As received fly ash (silica 58%) was chemically activated to increase alumina and was thought to be used for supporting potassium fluoride. The use of fly ash as support not only reduced the cost of the catalyst  it  also  showed   high   basicity  and  catalytic  activity  for  benzaldehyde  and  4-methoxybenzaldehyde with  2′-hydroxyacetophenone to produce 2′-hydroxychalcone and 4-methoxy-2′-hydroxychalcone  in  a  single   step,   liquid phase  and  solvent  free  reaction conditions with high yield (>90%) and purity. We also examined the changes in bulk and surface structures of KF/Al2O3-fly ash catalysts pretreated at different temperatures by XRD, FTIR, SEM-EDX and TEM to elucidate catalytically active sites formed by chemical and thermal treatment of fly ash.


## 2. Experimental

### 2.1. Material

Fly ash (Class F type with SiO2 and Al2O3 > 70%) used as solid support for the solid base was collected from Kota Thermal Power Plant (Rajasthan, India). α-Alumina, potassium fluoride (KF), aluminium nitrate (Al(NO3)3·9H2O), (NH4)2CO3, NH4OH,  benzaldehyde (99%), 4-methoxybenzaldehyde (98%) and 2′-hydroxyacetophenone (99%) were purchased from S. D. Fine Chem Ltd., India.


### 2.2. Catalyst Preparation

The three catalysts KF/fly ash, KF/Al2O3/fly ash and KF/Al2O3   were prepared by using aqueous solution of potassium fluoride for wet impregnation of fly ash, alumina enriched fly ash and α-alumina respectively. All three catalysts were calcined at different temperatures (473 K, 673 K, and 873 K) and prepared by the following method.


#### 2.2.1. KF/Fly Ash Catalyst

As received fly ash was preheated for 3 h at 900°C under static conditions. 10 g of thermally activated fly ash was added into a glass reactor containing aqueous solution of 0.166 g potassium fluoride (10 wt %). The reactor was equipped with a reflux condenser and a magnetic stirrer bar. The slurry was refluxed at 110°C for 24 h then filtered and washed to eliminate excess KF on the fly ash surface.


#### 2.2.2. KF/Al2O3/Fly Ash Catalyst

Step 1.
An aqueous solution of 0.09 mol of Al(NO3)3·3H2O was added into thermally activated fly ash with constant stirring. Solution of 0.16 mol of (NH4)2CO3  was added dropwise in the above solution and the pH was maintained close to 8.0 by the addition of appropriate amounts of NH4OH (35% aqueous ammonia solution). The resulting gel-like slurry was washed with deionized water until pH = 7. Then the precipitate was dried at 373 K in air for approximately 12 h. The resulting solid was calcined at 673 K for 4 h under static conditions.Step 2.
The chemically activated fly ash was heated at 400°C for 4 h prior to its introduction in a glass  reactor  containing  aqueous  solution  of 0.166 g  potassium  fluoride (10 wt%).  The reactor was equipped with a reflux condenser and a magnetic stirrer bar. The slurry was refluxed at 110°C for 24 h then filtered and washed to eliminate any excess KF on the fly ash surface.


#### 2.2.3. KF/Al2O3 Catalyst

10 g of alumina milled to a fine powder was added into deionized water containing desired amount of KF (0.166 g for 10 wt% loading). Thereafter the resulting solid products of all three catalysts were further dried at 110°C for 24 h and calcined at three different temperatures 473 K, 673 K and 873 K for 2 h.


### 2.3. Characterization

The samples were characterized by Fourier transform infrared spectroscopy (FTIR), powder X-ray diffraction study (XRD), BET surface area analysis, scanning electron microscopy (SEM) and transmission electron microscopy (TEM). The loading of KF on the chemically activated fly ash was confirmed by FTIR study using FTIR spectrophotometer (IRPrestige-21, Shimadzu) having a Diffuse Reflectance Scanning technique by mixing the sample with dried KBr (in 1/20 wt ratio) in the range of 400–4000 cm−1 with a resolution of 4 cm−1. X-ray diffraction studies were carried out by using X-ray diffractometer (Philips X’pert) with monochromatic CuKα radiation (λ=1.54056 Å) in a 2θ range of 5 to 65°. The detailed imaging information about the morphology and surface texture of the sample was provided by SEM-EDX (Philips XL30 ESEM TMP). The loading of KF on fly ash particles was confirmed by TEM analysis (Tecnai 20 G2 (FEI make), Resolution: Line-1.4 A, Point 2.04 A).


### 2.4. Reaction Procedure: Claisen-Schmidt Condensation

Catalytic activity of prepared catalysts was tested  by  Claisen-Schmidt  condensation  of benzaldehyde  and  4-methoxybenzaldehyde  with 2′-hydroxyacetophenone  in  solvent  free liquid phase reaction shown in Scheme1.Scheme 1
Claisen-Schmidt condensation of (a) benzaldehyde and (b) 4-methoxybenzaldehyde with 2-hydroxyacetophenone over fly ash supported solid base catalysts.The condensation was performed in liquid phase batch reactor, which consists of 50 mL round bottom flask, magnetic stirrer and condenser. A mixture of benzaldehyde (0.106 g, 1 mmol) or 4-methoxybenzaldehyde (0.136 g, 1 mmol) and hydroxyacetophenone (0.136 g, 1 mmol) was taken in round bottom flask. The catalysts, activated at different temperatures for 2 h (substrate to catalyst ratio = 10), were added in the reaction mixture. At the end of the reaction, the catalyst was filtered and the reaction mixture was analyzed by Gas  Chromatography  (Dani  Master  GC)  having  a  flame  ionization  detector  and  HP-5 capillary column of 30 m length and 0.25 mm diameter, programmed oven temperature of   50–280°C and N2 (1.5 mL/min) as a carrier gas.


### 2.5. Catalyst Regeneration

The used catalyst (KF/Al2O3/fly ash673) was washed with acetone and dried in oven at 110°C for 12 h followed by activation at 450°C for 2 h before reuse in next reaction cycle under similar reaction conditions as earlier.


## 2.1. Material

Fly ash (Class F type with SiO2 and Al2O3 > 70%) used as solid support for the solid base was collected from Kota Thermal Power Plant (Rajasthan, India). α-Alumina, potassium fluoride (KF), aluminium nitrate (Al(NO3)3·9H2O), (NH4)2CO3, NH4OH,  benzaldehyde (99%), 4-methoxybenzaldehyde (98%) and 2′-hydroxyacetophenone (99%) were purchased from S. D. Fine Chem Ltd., India.


## 2.2. Catalyst Preparation

The three catalysts KF/fly ash, KF/Al2O3/fly ash and KF/Al2O3   were prepared by using aqueous solution of potassium fluoride for wet impregnation of fly ash, alumina enriched fly ash and α-alumina respectively. All three catalysts were calcined at different temperatures (473 K, 673 K, and 873 K) and prepared by the following method.


### 2.2.1. KF/Fly Ash Catalyst

As received fly ash was preheated for 3 h at 900°C under static conditions. 10 g of thermally activated fly ash was added into a glass reactor containing aqueous solution of 0.166 g potassium fluoride (10 wt %). The reactor was equipped with a reflux condenser and a magnetic stirrer bar. The slurry was refluxed at 110°C for 24 h then filtered and washed to eliminate excess KF on the fly ash surface.


### 2.2.2. KF/Al2O3/Fly Ash Catalyst

Step 1.
An aqueous solution of 0.09 mol of Al(NO3)3·3H2O was added into thermally activated fly ash with constant stirring. Solution of 0.16 mol of (NH4)2CO3  was added dropwise in the above solution and the pH was maintained close to 8.0 by the addition of appropriate amounts of NH4OH (35% aqueous ammonia solution). The resulting gel-like slurry was washed with deionized water until pH = 7. Then the precipitate was dried at 373 K in air for approximately 12 h. The resulting solid was calcined at 673 K for 4 h under static conditions.Step 2.
The chemically activated fly ash was heated at 400°C for 4 h prior to its introduction in a glass  reactor  containing  aqueous  solution  of 0.166 g  potassium  fluoride (10 wt%).  The reactor was equipped with a reflux condenser and a magnetic stirrer bar. The slurry was refluxed at 110°C for 24 h then filtered and washed to eliminate any excess KF on the fly ash surface.


### 2.2.3. KF/Al2O3 Catalyst

10 g of alumina milled to a fine powder was added into deionized water containing desired amount of KF (0.166 g for 10 wt% loading). Thereafter the resulting solid products of all three catalysts were further dried at 110°C for 24 h and calcined at three different temperatures 473 K, 673 K and 873 K for 2 h.


## 2.2.1. KF/Fly Ash Catalyst

As received fly ash was preheated for 3 h at 900°C under static conditions. 10 g of thermally activated fly ash was added into a glass reactor containing aqueous solution of 0.166 g potassium fluoride (10 wt %). The reactor was equipped with a reflux condenser and a magnetic stirrer bar. The slurry was refluxed at 110°C for 24 h then filtered and washed to eliminate excess KF on the fly ash surface.


## 2.2.2. KF/Al2O3/Fly Ash Catalyst

Step 1.
An aqueous solution of 0.09 mol of Al(NO3)3·3H2O was added into thermally activated fly ash with constant stirring. Solution of 0.16 mol of (NH4)2CO3  was added dropwise in the above solution and the pH was maintained close to 8.0 by the addition of appropriate amounts of NH4OH (35% aqueous ammonia solution). The resulting gel-like slurry was washed with deionized water until pH = 7. Then the precipitate was dried at 373 K in air for approximately 12 h. The resulting solid was calcined at 673 K for 4 h under static conditions.Step 2.
The chemically activated fly ash was heated at 400°C for 4 h prior to its introduction in a glass  reactor  containing  aqueous  solution  of 0.166 g  potassium  fluoride (10 wt%).  The reactor was equipped with a reflux condenser and a magnetic stirrer bar. The slurry was refluxed at 110°C for 24 h then filtered and washed to eliminate any excess KF on the fly ash surface.


## 2.2.3. KF/Al2O3 Catalyst

10 g of alumina milled to a fine powder was added into deionized water containing desired amount of KF (0.166 g for 10 wt% loading). Thereafter the resulting solid products of all three catalysts were further dried at 110°C for 24 h and calcined at three different temperatures 473 K, 673 K and 873 K for 2 h.


## 2.3. Characterization

The samples were characterized by Fourier transform infrared spectroscopy (FTIR), powder X-ray diffraction study (XRD), BET surface area analysis, scanning electron microscopy (SEM) and transmission electron microscopy (TEM). The loading of KF on the chemically activated fly ash was confirmed by FTIR study using FTIR spectrophotometer (IRPrestige-21, Shimadzu) having a Diffuse Reflectance Scanning technique by mixing the sample with dried KBr (in 1/20 wt ratio) in the range of 400–4000 cm−1 with a resolution of 4 cm−1. X-ray diffraction studies were carried out by using X-ray diffractometer (Philips X’pert) with monochromatic CuKα radiation (λ=1.54056 Å) in a 2θ range of 5 to 65°. The detailed imaging information about the morphology and surface texture of the sample was provided by SEM-EDX (Philips XL30 ESEM TMP). The loading of KF on fly ash particles was confirmed by TEM analysis (Tecnai 20 G2 (FEI make), Resolution: Line-1.4 A, Point 2.04 A).


## 2.4. Reaction Procedure: Claisen-Schmidt Condensation

Catalytic activity of prepared catalysts was tested  by  Claisen-Schmidt  condensation  of benzaldehyde  and  4-methoxybenzaldehyde  with 2′-hydroxyacetophenone  in  solvent  free liquid phase reaction shown in Scheme1.Scheme 1
Claisen-Schmidt condensation of (a) benzaldehyde and (b) 4-methoxybenzaldehyde with 2-hydroxyacetophenone over fly ash supported solid base catalysts.The condensation was performed in liquid phase batch reactor, which consists of 50 mL round bottom flask, magnetic stirrer and condenser. A mixture of benzaldehyde (0.106 g, 1 mmol) or 4-methoxybenzaldehyde (0.136 g, 1 mmol) and hydroxyacetophenone (0.136 g, 1 mmol) was taken in round bottom flask. The catalysts, activated at different temperatures for 2 h (substrate to catalyst ratio = 10), were added in the reaction mixture. At the end of the reaction, the catalyst was filtered and the reaction mixture was analyzed by Gas  Chromatography  (Dani  Master  GC)  having  a  flame  ionization  detector  and  HP-5 capillary column of 30 m length and 0.25 mm diameter, programmed oven temperature of   50–280°C and N2 (1.5 mL/min) as a carrier gas.


## 2.5. Catalyst Regeneration

The used catalyst (KF/Al2O3/fly ash673) was washed with acetone and dried in oven at 110°C for 12 h followed by activation at 450°C for 2 h before reuse in next reaction cycle under similar reaction conditions as earlier.


## 3. Results and Discussion

### 3.1. Characterization

Elemental analysis  of fly ash  and  all  three catalysts  (KF/fly ash,  KF/Al2O3/fly ash and KF/Al2O3) was  done by EDX, the results are summarized in Table 1. With increasing the pretreatment temperature, the contents of K and F increased to a small extent by pretreatment at 673 K and decreased by pretreatment at 873 K for all three samples.Table 1
EDX analysis of prepared catalysts at different pre-treatment temperatures.
Catalyst
Pre-treatmenttemperature (K)
K (at.%)
F (at.%)
Al (at.%)
O (at.%)
Fly ash
NIL
0.09
NIL
4.10
50.2
Al2O3/fly ash
673 K
0.09
NIL
9.2
57.6
KF/fly ash
473 K
2.3
1.7
4.7
56.7
673 K
2.7
1.8
4.8
56.9
873 K
2.2
1.3
4.8
56.8
KF/Al2O3/fly ash
473 K
8.5
11.3
9.2
52.4
673 K
9.1
12.1
9.4
51.9
873 K
8.1
11.7
9.3
52.0
KF/Al2O3
473 K
20.8
19.6
12.7
46.9
673 K
22.1
20.8
12.9
44.2
873 K
18.8
17.7
17.2
46.3
[at.%: atomic percentage].The FTIR spectrum of fly ash Figure1 shows a peak at 3600 cm−1, which indicates the presence of surface −OH groups, −Si-OH and absorbed water molecules on the surface. The spectra also shows a broad range of bands from 1055 cm−1 to 1100 cm−1 which is attributed to modes of Si-O-Si asymmetric band stretching vibrations. The low frequency modes at 794 cm−1 are due to the symmetric Si-O-Si stretching vibrations.  The FTIR spectrum of KF/Al2O3/fly ash catalyst calcined at different temperatures (43 K, 673 K, and 873 K) shown in Figures 1(d), 1(e) and 1(f). The FTIR spectrum of KF/Al2O3/fly ash673 catalyst, shown in Figure 1(e) has a strong band at about 3500 cm−1,which indicates the presence of –OH groups on the surface of KF/Al2O3/fly ash673  catalyst. Thus result shows that hydroxyl groups can be the active sites when KF is supported on fly ash [27]. The  intensity  of  the  −OH  peak  increases  with increasing temperature from  473 K to 673 K, assigned due to increase in KF content. Upon investigating the nature of the catalyst via infrared spectroscopic studies of the catalyst surface, it became apparent that fluoride ion has little or no direct role in the enhanced reactivity of KF/Al2O3/fly ash catalyst. The reaction between aqueous KF and alumina results in the formation of potassium hexafluoroaluminate and a strongly basic surface consisting of potassium aluminates and potassium hydroxide [28]. The later agents are responsible for both the increased base activity and the variable activity, a consequence of carbonate formation. A peak is present at 1650 cm−1 in the spectra of the samples, which   is attributed to bending mode (δO−H) of water molecule [5]. An intense band at 570 cm−1 is also observed which is due to the presence of substantial amount of hexafluoroaluminate ion. In addition to features due to alumina and water, bands at 1519 cm−1 and 1381 cm−1 indicate that  both  bidentate and monodentate  type  carbonate  species  exist  on  the  surface  of KF/Al2O3/fly ash673   catalyst  [5, 29], which  seems  to  be  generated  due  to  reaction  of atmospheric CO2  with KOH during drying of the catalyst.Figure 1
FTIR of (a) raw fly ash, (b) thermally activated fly ash, (c) KF/fly ash catalyst, (d) KF/Al2O3/fly ash873 catalyst, (e) KF/Al2O3/fly ash673 vatalyst, (f) KF/Al2O3/fly ash473 catalyst, and (g) regenerated KF/Al2O3/fly ash673 catalyst.X-ray diffraction pattern of raw fly ash is shown in Figure2(a). Structural changes caused by pretreatment at different temperatures were studied by XRD for  KF/Al2O3/fly ash473, KF/Al2O3/fly ash673, and KF/Al2O3/fly ash873 catalysts illustrated in Figures 2(b), 2(c) and 2(d). These patterns confirmed that deposition of the alkaline fluoride followed by the thermal treatment led to the formation of K3AlF6  by the reaction between KF and Al2O3 which is observed at 2 theta = 33°, 38°, and 63°. The intensity of the peaks assigned to this species is in agreement with the loadings of the alkaline fluoride [30].X-ray diffraction pattern of (a) raw fly ash (b) KF/Al2O3/fly ash473 catalyst (c) KF/Al2O3/fly ash873 and (d) KF/Al2O3/fly ash673 catalyst.
(a)
(b)
(c)
(d)SEM micrograph of raw fly ash Figure3(a) shows the presence of hollow cenospheres, irregularly shaped unburned carbon particles, mineral aggregates and agglomerated particles, while the typical SEM images of the fly ash supported KF catalyst in Figure 3(b) show dense particles with distribution of varying particle size. TEM images of raw fly ash Figure 4(a) show smooth spherical particles, while TEM image of KF/Al2O3/fly ash673 catalyst Figure 4(b) shows KF loaded spheres.SEM micrograph of (a) Raw fly ash and (b) KF/Al2O3/fly ash673 catalyst.
(a)
(b)TEM image of (a) Raw fly ash and (b) KF/Al2O3/fly ash673 catalyst.
(a)
(b)


### 3.2. Basic Sites on KF/Al2O3/Fly Ash Catalyst

There are several controversies on possibilities of formation of basic sites on KF/Al2O3 catalytic system, yet all the previous investigations [27] evidently reported the formation of K3AlF6 by the reaction of aqueous KF and alumina (1). Most of the studies were of the opinion that F− ion has no direct role in the catalytic activity of KF/Al2O3. The formation of carbonate on the catalyst surface is responsible for high reactivity of KF/Al2O3 [28]. The carbonate was supposed to be formed by the reaction of CO2 and produced KOH (2) during the drying procedure:
(2)4KOH+2CO2⟶2K2CO3+2H2O
Duke et al. has reported the formation of K2CO3 by the following successive reactions:
(3)12KF+Al2O3⟶2K3AlF6+K2O(4)3K2O+3CO2⟶3K2CO3
where K2O is formed as the alumina lattice is destroyed. However in preparation of the KF/Al2O3/fly ash catalyst in aqueous medium (2) seems to be more significant than (3) and (4).In KF/Al2O3/fly ash catalyst, the formation of K3AlF6 is confirmed by XRD, while hydroxyl groups and carbonate ion are confirmed by intense peaks at 3500 cm−1and 1550 cm−1 in FTIR spectrum Figure 1. Interestingly, the pretreatment temperature has significantly affected the catalytic activity of the system as reported previously for KF/Al2O3  catalyst. Both K3AlF6 and carbonate peaks are observed on increasing the pretreatment temperature from 473 K to 873 K as evident from Figure 1, whereas the catalytic activity of KF/Al2O3/fly ash catalyst was almost diminished at higher temperature 873 K Figure 5(a). These results have ruled out the possibility of carbonate or K3AlF6 being responsible for generating the active basic sites on the catalyst surface. KOH, an active base produced during reaction between KF and alumina generates hydroxyl groups on the catalyst surface, which become active basic sites for condensation reactions. At 873 K, surface hydroxyl groups are significantly decreased, resulting in decrease of active basic sites; thus catalytic activity of KF/Al2O3/fly ash catalyst was almost completely lost. Similar explanations on the surface properties of KF/Al2O3 system have been given in the literature [5] where the catalytic activity of KF/ Al2O3   was completely lost.Conversion (%) of benzaldehyde and 4-methoxybenzaldehyde with KF/Al2O3/fly  ash catalyst at (a) different pretreatment temperature (b) different reaction temperature (c) different time (d) different reaction cycles and (e) different molar ratios of benzaldehyde and 4-methoxybenzaldehyde.
(a)
(b)
(c)
(d)
(e)


### 3.3. Catalytic Performance

The catalytic activity of KF/Al2O3/fly ash depends very much on drying condition of alumina after loading KF by impregnation. In this work we examined the dependence of catalytic activity for condensation on the heating temperature of the catalyst.


#### 3.3.1. Effect of Pretreatment Temperature

The catalytic activity strongly depends on the evacuation temperature and reached around a maximum temperature of 673 K Figure5(a).  All catalysts showed significant activity for condensation reactions, whereas pure fly ash and chemically activated fly ash (Al2O3/fly ash) did not show any activity. Among remaining catalysts, the KF/Al2O3/fly ash673 showed higher catalytic activity giving  maximum  conversion  of  benzaldehyde  (83%) and 4-methoxybenzaldehyde  (89%).  For KF/Al2O3/fly ash473 and KF/Al2O3/fly ash873, conversions of benzaldehyde and 4-methoxybenzaldehyde are comparatively low as shown in Figure 5(a). The activity of KF/Al2O3/fly ash catalyst appeared when the sample was pretreated at 473 K and reached its maximum at the temperature of 673 K. As the pretreatment temperature was raised higher than 673 K, the activity decreased sharply and finally disappeared at the temperature of 873 K. It is well reported that a high temperature treatment reveals active sites on catalyst either by removal of CO2 and H2O remaining on the surface in various forms or by formation of specific surface structure. The active sites are covered with H2O and/or CO2 when pretreated below 673 K [7].In the light of the above inferences, the reaction conditions such as reaction temperature, reaction time, molar ratio of reactants and substrate to catalyst ratio for condensation of benzaldehyde and 4-methoxybenzaldehyde with 2′-hydroxyacetophenone were optimized using only KF/Al2O3/fly ash673 catalyst.


#### 3.3.2. Effect of Temperature

The reaction for condensation of benzaldehyde and 4-methoxybenzaldehyde is carried out at temperatures ranging from 40°C to 140°C for 4 h.  The effect of temperature on the condensation activity of KF/Al2O3/fly ash673 and kinetics is shown in Figure 5(b). It can be seen that at 80°C the conversion of benzaldehyde is 68% and increases to 83% at 120°C for a reaction time of 4 h, which remains constant till 140°C. Similarly, conversion of 4-methoxy benzaldehyde is maximum 89% at 140°C.


#### 3.3.3. Effect of Reaction Time

The optimum reaction time required, achieving maximum conversion of benzaldehyde and 4-methoxybenzaldehyde is carried out at 40 and 140°C for different time intervals from 30 min to 8 h. The conversion of benzaldehyde and 4-methoxybenzaldehyde gradually increases with time giving 83% and 89% after 4 h respectively as given in Figure5(c) which remains constant till 8 h.


#### 3.3.4. Effect of Molar Ratio (Substrate/2′-hydroxyacetophenone)

The effect   of   the   molar   ratio   of   benzaldehyde   to   2′-hydroxyacetophenone   and 4-methoxybenzaldehyde to 2′-hydroxyacetophenone on conversion and yield of products is also studied at a reaction temperature of 120°C and 140°C and reaction time 4 h. At the molar ratio of 1 : 1, maximum conversion of benzaldehyde and 4-methoxybenzaldehyde with yield of their respective products was obtained (Figure5(e)). With increasing the molar ratio, the conversion was observed to be decreased, which can be attributed to formation of benzoic acid as side product.


### 3.4. Comparison of Catalytic Activity of KF/Al2O3/Fly Ash with the Literature Data

The reaction between 2′-hydroxyacetophenone   and benzaldehyde has been carried out over different catalysts as reported in the literature. The results obtained from the reported catalysts showed that when zeolite NaX and a sepiolite partially exchanged with Cs were used as catalysts, their activity was very low [31]. It is because of the fact that H atoms present in the methyl group of acetophenone has high pKa value (15.8) and it has been demonstrated previously that the basic sites of exchanged CsNaX and Cs sepiolite catalysts can only  abstract proton with pKa = 10.7 and 13.3 respectively [31]. So it is evident from the above results that a catalyst with strong basic sites should be used to get the high conversion value. It is also reported when an excess of Cs is exchanged with zeolite, it can give completely high conversion, but the catalyst have to be use in the inert atmosphere, in order to avoid the formation of carbonates [32]. Mg-Al hydrotalcite derived catalyst has also been used in this reaction and a conversion of 78% was obtained [33]. The presence of water also affects the conversion value. Similarly reaction between 4-methoxybenzaldehyde and 2′-hydroxyacetophenone   in the presence of MeOH/KOH at room temperature gives 65 % yield of 4-methoxy-2′-hydroxychalcone in 24 h [34].In order to find the optimum for the studied reactions, we have synthesized highly basic KF/Al2O3/fly ash catalyst and it is found that with this catalyst the conversion value (83%) of benzaldehyde and (89%) of 4-methoxybenzaldehyde was increased. The prepared catalyst is also reused for up to three reaction cycles. The regenerated  catalyst showed similar catalytic  activity till 3rd reaction cycle giving approximately   similar conversion of benzaldehyde  (81%)  and  4-methoxybenzaldehyde (86%),  which  indicates  that  the  sites  are  not  deactivated  in  the  regenerated  catalyst  as confirmed  by  FTIR  of  regenerated  catalyst   (Figure 1(g)).


### 3.5. Characterization of Products

NMR of 2′-hydroxychalcone: H1-NMR (200 MHz, CDCl3), δ ppm: 12.78 (s, 1H, 2′-OH), 7.91−7.96 (d, 1H, J=7.6 Hz, and 1.8 Hz, H6′) 7.91−7.96 (dd, 1H, J=14.4 Hz, Hβ), 7.35−7.70 (m, 7H,  Hα, H4′, H2, H3, H4, H5, and H6) and 7.02−7.09 (m, 2H, H3′, and H5′). NMR of 4-methoxy-2′-hydroxychalcone: H1-NMR (200 MHz, CDCl3), δ ppm: 12.95 (s, 1H, 2′-OH), 7.88−7.96 (d, 1H, J=15.2 Hz, Hβ), 7.87−7.91 (d, 1H, J=7.4 Hz, H6′)   7.59−7.66 (d, 1H, J=15.2 Hz, Hα) 7.62−7.66 (d, 2H, J=8.8 Hz, H2 and H6) 7.45−7.49 (t, 1H, J=8.8 Hz, and 7.6 Hz, H4′) 6.90−7.05 (m, 4H, H3, H5, H3′ and 5′ h) and 3.87 (s, 3H, OCH3).


## 3.1. Characterization

Elemental analysis  of fly ash  and  all  three catalysts  (KF/fly ash,  KF/Al2O3/fly ash and KF/Al2O3) was  done by EDX, the results are summarized in Table 1. With increasing the pretreatment temperature, the contents of K and F increased to a small extent by pretreatment at 673 K and decreased by pretreatment at 873 K for all three samples.Table 1
EDX analysis of prepared catalysts at different pre-treatment temperatures.
Catalyst
Pre-treatmenttemperature (K)
K (at.%)
F (at.%)
Al (at.%)
O (at.%)
Fly ash
NIL
0.09
NIL
4.10
50.2
Al2O3/fly ash
673 K
0.09
NIL
9.2
57.6
KF/fly ash
473 K
2.3
1.7
4.7
56.7
673 K
2.7
1.8
4.8
56.9
873 K
2.2
1.3
4.8
56.8
KF/Al2O3/fly ash
473 K
8.5
11.3
9.2
52.4
673 K
9.1
12.1
9.4
51.9
873 K
8.1
11.7
9.3
52.0
KF/Al2O3
473 K
20.8
19.6
12.7
46.9
673 K
22.1
20.8
12.9
44.2
873 K
18.8
17.7
17.2
46.3
[at.%: atomic percentage].The FTIR spectrum of fly ash Figure1 shows a peak at 3600 cm−1, which indicates the presence of surface −OH groups, −Si-OH and absorbed water molecules on the surface. The spectra also shows a broad range of bands from 1055 cm−1 to 1100 cm−1 which is attributed to modes of Si-O-Si asymmetric band stretching vibrations. The low frequency modes at 794 cm−1 are due to the symmetric Si-O-Si stretching vibrations.  The FTIR spectrum of KF/Al2O3/fly ash catalyst calcined at different temperatures (43 K, 673 K, and 873 K) shown in Figures 1(d), 1(e) and 1(f). The FTIR spectrum of KF/Al2O3/fly ash673 catalyst, shown in Figure 1(e) has a strong band at about 3500 cm−1,which indicates the presence of –OH groups on the surface of KF/Al2O3/fly ash673  catalyst. Thus result shows that hydroxyl groups can be the active sites when KF is supported on fly ash [27]. The  intensity  of  the  −OH  peak  increases  with increasing temperature from  473 K to 673 K, assigned due to increase in KF content. Upon investigating the nature of the catalyst via infrared spectroscopic studies of the catalyst surface, it became apparent that fluoride ion has little or no direct role in the enhanced reactivity of KF/Al2O3/fly ash catalyst. The reaction between aqueous KF and alumina results in the formation of potassium hexafluoroaluminate and a strongly basic surface consisting of potassium aluminates and potassium hydroxide [28]. The later agents are responsible for both the increased base activity and the variable activity, a consequence of carbonate formation. A peak is present at 1650 cm−1 in the spectra of the samples, which   is attributed to bending mode (δO−H) of water molecule [5]. An intense band at 570 cm−1 is also observed which is due to the presence of substantial amount of hexafluoroaluminate ion. In addition to features due to alumina and water, bands at 1519 cm−1 and 1381 cm−1 indicate that  both  bidentate and monodentate  type  carbonate  species  exist  on  the  surface  of KF/Al2O3/fly ash673   catalyst  [5, 29], which  seems  to  be  generated  due  to  reaction  of atmospheric CO2  with KOH during drying of the catalyst.Figure 1
FTIR of (a) raw fly ash, (b) thermally activated fly ash, (c) KF/fly ash catalyst, (d) KF/Al2O3/fly ash873 catalyst, (e) KF/Al2O3/fly ash673 vatalyst, (f) KF/Al2O3/fly ash473 catalyst, and (g) regenerated KF/Al2O3/fly ash673 catalyst.X-ray diffraction pattern of raw fly ash is shown in Figure2(a). Structural changes caused by pretreatment at different temperatures were studied by XRD for  KF/Al2O3/fly ash473, KF/Al2O3/fly ash673, and KF/Al2O3/fly ash873 catalysts illustrated in Figures 2(b), 2(c) and 2(d). These patterns confirmed that deposition of the alkaline fluoride followed by the thermal treatment led to the formation of K3AlF6  by the reaction between KF and Al2O3 which is observed at 2 theta = 33°, 38°, and 63°. The intensity of the peaks assigned to this species is in agreement with the loadings of the alkaline fluoride [30].X-ray diffraction pattern of (a) raw fly ash (b) KF/Al2O3/fly ash473 catalyst (c) KF/Al2O3/fly ash873 and (d) KF/Al2O3/fly ash673 catalyst.
(a)
(b)
(c)
(d)SEM micrograph of raw fly ash Figure3(a) shows the presence of hollow cenospheres, irregularly shaped unburned carbon particles, mineral aggregates and agglomerated particles, while the typical SEM images of the fly ash supported KF catalyst in Figure 3(b) show dense particles with distribution of varying particle size. TEM images of raw fly ash Figure 4(a) show smooth spherical particles, while TEM image of KF/Al2O3/fly ash673 catalyst Figure 4(b) shows KF loaded spheres.SEM micrograph of (a) Raw fly ash and (b) KF/Al2O3/fly ash673 catalyst.
(a)
(b)TEM image of (a) Raw fly ash and (b) KF/Al2O3/fly ash673 catalyst.
(a)
(b)


## 3.2. Basic Sites on KF/Al2O3/Fly Ash Catalyst

There are several controversies on possibilities of formation of basic sites on KF/Al2O3 catalytic system, yet all the previous investigations [27] evidently reported the formation of K3AlF6 by the reaction of aqueous KF and alumina (1). Most of the studies were of the opinion that F− ion has no direct role in the catalytic activity of KF/Al2O3. The formation of carbonate on the catalyst surface is responsible for high reactivity of KF/Al2O3 [28]. The carbonate was supposed to be formed by the reaction of CO2 and produced KOH (2) during the drying procedure:
(2)4KOH+2CO2⟶2K2CO3+2H2O
Duke et al. has reported the formation of K2CO3 by the following successive reactions:
(3)12KF+Al2O3⟶2K3AlF6+K2O(4)3K2O+3CO2⟶3K2CO3
where K2O is formed as the alumina lattice is destroyed. However in preparation of the KF/Al2O3/fly ash catalyst in aqueous medium (2) seems to be more significant than (3) and (4).In KF/Al2O3/fly ash catalyst, the formation of K3AlF6 is confirmed by XRD, while hydroxyl groups and carbonate ion are confirmed by intense peaks at 3500 cm−1and 1550 cm−1 in FTIR spectrum Figure 1. Interestingly, the pretreatment temperature has significantly affected the catalytic activity of the system as reported previously for KF/Al2O3  catalyst. Both K3AlF6 and carbonate peaks are observed on increasing the pretreatment temperature from 473 K to 873 K as evident from Figure 1, whereas the catalytic activity of KF/Al2O3/fly ash catalyst was almost diminished at higher temperature 873 K Figure 5(a). These results have ruled out the possibility of carbonate or K3AlF6 being responsible for generating the active basic sites on the catalyst surface. KOH, an active base produced during reaction between KF and alumina generates hydroxyl groups on the catalyst surface, which become active basic sites for condensation reactions. At 873 K, surface hydroxyl groups are significantly decreased, resulting in decrease of active basic sites; thus catalytic activity of KF/Al2O3/fly ash catalyst was almost completely lost. Similar explanations on the surface properties of KF/Al2O3 system have been given in the literature [5] where the catalytic activity of KF/ Al2O3   was completely lost.Conversion (%) of benzaldehyde and 4-methoxybenzaldehyde with KF/Al2O3/fly  ash catalyst at (a) different pretreatment temperature (b) different reaction temperature (c) different time (d) different reaction cycles and (e) different molar ratios of benzaldehyde and 4-methoxybenzaldehyde.
(a)
(b)
(c)
(d)
(e)


## 3.3. Catalytic Performance

The catalytic activity of KF/Al2O3/fly ash depends very much on drying condition of alumina after loading KF by impregnation. In this work we examined the dependence of catalytic activity for condensation on the heating temperature of the catalyst.


### 3.3.1. Effect of Pretreatment Temperature

The catalytic activity strongly depends on the evacuation temperature and reached around a maximum temperature of 673 K Figure5(a).  All catalysts showed significant activity for condensation reactions, whereas pure fly ash and chemically activated fly ash (Al2O3/fly ash) did not show any activity. Among remaining catalysts, the KF/Al2O3/fly ash673 showed higher catalytic activity giving  maximum  conversion  of  benzaldehyde  (83%) and 4-methoxybenzaldehyde  (89%).  For KF/Al2O3/fly ash473 and KF/Al2O3/fly ash873, conversions of benzaldehyde and 4-methoxybenzaldehyde are comparatively low as shown in Figure 5(a). The activity of KF/Al2O3/fly ash catalyst appeared when the sample was pretreated at 473 K and reached its maximum at the temperature of 673 K. As the pretreatment temperature was raised higher than 673 K, the activity decreased sharply and finally disappeared at the temperature of 873 K. It is well reported that a high temperature treatment reveals active sites on catalyst either by removal of CO2 and H2O remaining on the surface in various forms or by formation of specific surface structure. The active sites are covered with H2O and/or CO2 when pretreated below 673 K [7].In the light of the above inferences, the reaction conditions such as reaction temperature, reaction time, molar ratio of reactants and substrate to catalyst ratio for condensation of benzaldehyde and 4-methoxybenzaldehyde with 2′-hydroxyacetophenone were optimized using only KF/Al2O3/fly ash673 catalyst.


### 3.3.2. Effect of Temperature

The reaction for condensation of benzaldehyde and 4-methoxybenzaldehyde is carried out at temperatures ranging from 40°C to 140°C for 4 h.  The effect of temperature on the condensation activity of KF/Al2O3/fly ash673 and kinetics is shown in Figure 5(b). It can be seen that at 80°C the conversion of benzaldehyde is 68% and increases to 83% at 120°C for a reaction time of 4 h, which remains constant till 140°C. Similarly, conversion of 4-methoxy benzaldehyde is maximum 89% at 140°C.


### 3.3.3. Effect of Reaction Time

The optimum reaction time required, achieving maximum conversion of benzaldehyde and 4-methoxybenzaldehyde is carried out at 40 and 140°C for different time intervals from 30 min to 8 h. The conversion of benzaldehyde and 4-methoxybenzaldehyde gradually increases with time giving 83% and 89% after 4 h respectively as given in Figure5(c) which remains constant till 8 h.


### 3.3.4. Effect of Molar Ratio (Substrate/2′-hydroxyacetophenone)

The effect   of   the   molar   ratio   of   benzaldehyde   to   2′-hydroxyacetophenone   and 4-methoxybenzaldehyde to 2′-hydroxyacetophenone on conversion and yield of products is also studied at a reaction temperature of 120°C and 140°C and reaction time 4 h. At the molar ratio of 1 : 1, maximum conversion of benzaldehyde and 4-methoxybenzaldehyde with yield of their respective products was obtained (Figure5(e)). With increasing the molar ratio, the conversion was observed to be decreased, which can be attributed to formation of benzoic acid as side product.


## 3.3.1. Effect of Pretreatment Temperature

The catalytic activity strongly depends on the evacuation temperature and reached around a maximum temperature of 673 K Figure5(a).  All catalysts showed significant activity for condensation reactions, whereas pure fly ash and chemically activated fly ash (Al2O3/fly ash) did not show any activity. Among remaining catalysts, the KF/Al2O3/fly ash673 showed higher catalytic activity giving  maximum  conversion  of  benzaldehyde  (83%) and 4-methoxybenzaldehyde  (89%).  For KF/Al2O3/fly ash473 and KF/Al2O3/fly ash873, conversions of benzaldehyde and 4-methoxybenzaldehyde are comparatively low as shown in Figure 5(a). The activity of KF/Al2O3/fly ash catalyst appeared when the sample was pretreated at 473 K and reached its maximum at the temperature of 673 K. As the pretreatment temperature was raised higher than 673 K, the activity decreased sharply and finally disappeared at the temperature of 873 K. It is well reported that a high temperature treatment reveals active sites on catalyst either by removal of CO2 and H2O remaining on the surface in various forms or by formation of specific surface structure. The active sites are covered with H2O and/or CO2 when pretreated below 673 K [7].In the light of the above inferences, the reaction conditions such as reaction temperature, reaction time, molar ratio of reactants and substrate to catalyst ratio for condensation of benzaldehyde and 4-methoxybenzaldehyde with 2′-hydroxyacetophenone were optimized using only KF/Al2O3/fly ash673 catalyst.


## 3.3.2. Effect of Temperature

The reaction for condensation of benzaldehyde and 4-methoxybenzaldehyde is carried out at temperatures ranging from 40°C to 140°C for 4 h.  The effect of temperature on the condensation activity of KF/Al2O3/fly ash673 and kinetics is shown in Figure 5(b). It can be seen that at 80°C the conversion of benzaldehyde is 68% and increases to 83% at 120°C for a reaction time of 4 h, which remains constant till 140°C. Similarly, conversion of 4-methoxy benzaldehyde is maximum 89% at 140°C.


## 3.3.3. Effect of Reaction Time

The optimum reaction time required, achieving maximum conversion of benzaldehyde and 4-methoxybenzaldehyde is carried out at 40 and 140°C for different time intervals from 30 min to 8 h. The conversion of benzaldehyde and 4-methoxybenzaldehyde gradually increases with time giving 83% and 89% after 4 h respectively as given in Figure5(c) which remains constant till 8 h.


## 3.3.4. Effect of Molar Ratio (Substrate/2′-hydroxyacetophenone)

The effect   of   the   molar   ratio   of   benzaldehyde   to   2′-hydroxyacetophenone   and 4-methoxybenzaldehyde to 2′-hydroxyacetophenone on conversion and yield of products is also studied at a reaction temperature of 120°C and 140°C and reaction time 4 h. At the molar ratio of 1 : 1, maximum conversion of benzaldehyde and 4-methoxybenzaldehyde with yield of their respective products was obtained (Figure5(e)). With increasing the molar ratio, the conversion was observed to be decreased, which can be attributed to formation of benzoic acid as side product.


## 3.4. Comparison of Catalytic Activity of KF/Al2O3/Fly Ash with the Literature Data

The reaction between 2′-hydroxyacetophenone   and benzaldehyde has been carried out over different catalysts as reported in the literature. The results obtained from the reported catalysts showed that when zeolite NaX and a sepiolite partially exchanged with Cs were used as catalysts, their activity was very low [31]. It is because of the fact that H atoms present in the methyl group of acetophenone has high pKa value (15.8) and it has been demonstrated previously that the basic sites of exchanged CsNaX and Cs sepiolite catalysts can only  abstract proton with pKa = 10.7 and 13.3 respectively [31]. So it is evident from the above results that a catalyst with strong basic sites should be used to get the high conversion value. It is also reported when an excess of Cs is exchanged with zeolite, it can give completely high conversion, but the catalyst have to be use in the inert atmosphere, in order to avoid the formation of carbonates [32]. Mg-Al hydrotalcite derived catalyst has also been used in this reaction and a conversion of 78% was obtained [33]. The presence of water also affects the conversion value. Similarly reaction between 4-methoxybenzaldehyde and 2′-hydroxyacetophenone   in the presence of MeOH/KOH at room temperature gives 65 % yield of 4-methoxy-2′-hydroxychalcone in 24 h [34].In order to find the optimum for the studied reactions, we have synthesized highly basic KF/Al2O3/fly ash catalyst and it is found that with this catalyst the conversion value (83%) of benzaldehyde and (89%) of 4-methoxybenzaldehyde was increased. The prepared catalyst is also reused for up to three reaction cycles. The regenerated  catalyst showed similar catalytic  activity till 3rd reaction cycle giving approximately   similar conversion of benzaldehyde  (81%)  and  4-methoxybenzaldehyde (86%),  which  indicates  that  the  sites  are  not  deactivated  in  the  regenerated  catalyst  as confirmed  by  FTIR  of  regenerated  catalyst   (Figure 1(g)).


## 3.5. Characterization of Products

NMR of 2′-hydroxychalcone: H1-NMR (200 MHz, CDCl3), δ ppm: 12.78 (s, 1H, 2′-OH), 7.91−7.96 (d, 1H, J=7.6 Hz, and 1.8 Hz, H6′) 7.91−7.96 (dd, 1H, J=14.4 Hz, Hβ), 7.35−7.70 (m, 7H,  Hα, H4′, H2, H3, H4, H5, and H6) and 7.02−7.09 (m, 2H, H3′, and H5′). NMR of 4-methoxy-2′-hydroxychalcone: H1-NMR (200 MHz, CDCl3), δ ppm: 12.95 (s, 1H, 2′-OH), 7.88−7.96 (d, 1H, J=15.2 Hz, Hβ), 7.87−7.91 (d, 1H, J=7.4 Hz, H6′)   7.59−7.66 (d, 1H, J=15.2 Hz, Hα) 7.62−7.66 (d, 2H, J=8.8 Hz, H2 and H6) 7.45−7.49 (t, 1H, J=8.8 Hz, and 7.6 Hz, H4′) 6.90−7.05 (m, 4H, H3, H5, H3′ and 5′ h) and 3.87 (s, 3H, OCH3).


## 4. Conclusion

The study provides KF/Al2O3/fly ash as an efficient solid base catalyst possessing significant amount of basicity.  The chemical activation of fly ash by alumina results in increased amorphous alumina content and thus surface hydroxyl contents produced due to the reaction of KF and alumina on fly ash support. Among all catalysts, KF/Al2O3/fly ash catalyst shows high catalytic activity towards condensation reaction. The experimental results indicate that the basicity of supported KF can be significantly increased by a proper choice of support. In KF/Al2O3/fly  ash  catalysts,  KF  reacts  with  alumina  of  fly  ash  and  forms potassium hexafluoroaluminate and hydroxide, as the major phase which increases with increase in calcination temperature from 473 K to 673 K, responsible for enhancement of reactivity of catalyst.  Along  with  these  species,  bidentate  carbonate  species  exist  on  the  surface  of KF/Al2O3/fly ash673 catalyst which is formed by the formation of K2CO3. The KF/Al2O3/fly ash catalysts were found active for condensation of benzaldehyde and 4-methoxybenzaldehyde with 2′-hydroxyacetophenone, in which KF/Al2O3/fly ash pretreated  at  673 K  gave  higher  conversion  of  benzaldehyde  (87%)  with  91%  yield  of 2′- hydroxychalcone  and 4-methoxybenzaldehyde  (93%)  with  93%  yield  of  4-methoxy-2′-hydroxychalcone. Experimental results also indicate that the basicity generated over only KF/fly ash catalyst was not sufficient to get higher yield of condensation products, but when fly ash was chemically activated by loading alumina through precipitation using aluminium nitrate as precursor, KF/Al2O3/fly ash catalyst has shown increased catalytic activity for the same reaction. The conversion (83% and 89%) of benzaldehyde and 4-methoxybenzaldehyde in  KF/Al2O3/fly  ash  catalytic  system  was   comparable  to  the  only  KF/Al2O3 system (conversion 61% and 59%) however, the cost of the  KF/Al2O3/fly ash is lower than the KF/Al2O3, due to the replacement of α-alumina support by alumina/fly ash support. Fly ash already has 17 wt% alumina and by chemically activating it with aluminium nitrate, the alumina content was increased up to 37 wt%, which is found to be responsible for generating sufficient basic sites to catalyze the Claisen-Schmidt condensation. This catalyst may further be explored for several other organic transformations.Recycling experiments showed that the catalyst is very stable up to three cycles. A composite material which can combine the advantages of fly ash, alumina and KF can expand the catalytic capabilities of the material especially in applications as strong base catalysts for industrially important reactions.



---

*Source: 723957-2013-07-01.xml*