Indian Journal of Chemical Technology Vol 3, September 1996, pp. 253-255 A comparison of catalytic activity of zeolites with some Lewis acids in esterification reaction N Nagaraju· & P Mehboob Department of Chemistry, St Joseph's College, P.O. Centre, 46, Langford Road, Bangalore, 560 027, India Received 24 July 1995; accepted 13 February 1996 In this paper, an attempt has been made to compare the catalytic activity of zeolites of the types NaX, NaY and NaZSM-S and their protonated forms with some conventional Lewis acids such as anhydrous ZnCI2, AlCl3 and H2S04 in the esterification reaction between isoamyl alcohol and acetic acid in liquid phase. The product has been analysed by chemical methods and confirmed· by FTIR and IH NMR spectral studies. The percentage of ester in the reaction product has been estimated using gas chromatographic technique. It is observed that zeolites are more active than the conventional Lewis acids in catalysing this reaction and among the zeolites HZSM-5 resulted in 100% yield of the ester in the product extract. Selectivityfor eSterformation has also been found to be 100%. Esters are valuable. starting materials in the synthesis of complex organic molecules1 and widely used as industrial solvents for paints. Industrially esters are synthesised by direct esterification with sulphuric acid as the catalyst. However, this synthetic method has several drawbacks2, i.e., (i) sulphuric acid can cause several side reactions and decreases the Yield of ester and (ii) corrosion of the equipment used is so severe by strong acid that etched parts have to be replaced frequently resulting in the rise of operation cost considerably. There has· been a considerable amount of interest in using solid acids such as metal oxides3• zoolites4 and clays5 as catalysts in many industrially important acid catalysed reactions. These materials possess several advantages over conventional Lewis acids6, for instance (a) less or no corrosion, (b) no waste or disposal problems, (c) setting up of continuous process in fixed bed reactions easily and (d) high thermal stability. Catalytic activity of the solid acids in most of the industrially important reactions has been investigated in vapour phase usin~ fixed bed reaCtors. Only a few papers have appeared on the use of solid acids in liquid phase reactions 7 - 9• In the present investigation, an attempt has been made to find out the catalytic activity of zeolites in esterification reaction between acetic acid and isoamyl alcohol in liquid phase and compare their activity with the conventional Lewis acids. •Author to whom corres~ should be addressed. Experimental Procedure Reagents and catalysts-Synthetic grade isoamyl alcohol, glacial acetic acid and laboratory grade aIlhydrous ZnCI2, AlCl3 and conc. H2S04 were used in this investigation. The catalysts aIlhydrous ZnCI2, AlCl3 and conc. H2S04 were used as such. Zeolite samples of type NaX, NaY and NaZSM-5 (Si/ Al ratio = 1, 3 and 75 respectively) were supplied by IPCL, Baroda. Sodium forms of the zeolites were converted into their H-form using NH4N03 (15 cm3 of 10% solution per gram of the zeolite) following standard procedures. These H-form of the zeolites are designated' as HX, HY andHZSM-5. Catalytic activity studies-Catalytic activity of the solid catalysts in the esterificationI'eaction between isoamyl alcohol and acetic acid in liquid phase was studied both at room and refluxing temperatures. A mixture of the alcohol and the acid (25 cm3 in 1:1 molar ratio) was miXed with 2 g of the catalyst. The zeolites were activated at 500°C for 6 h before using them in the reaction. The reaction mixture was refluxed for 20 h over a mantle using water cooled condensor. After the Specified time reaction mixture was cooled and the· product formed was separated as per the procedure described elsewhere10. Analysis of the products-The product extracts from various reactions carried out with different catalysts were analysed and the presence of ester was confirmed. IR and 1H-NMRspectra of a 'few product samples (sample nps. 1, 2, 5, 9, as given in Table 1) and an authentic sample of isoamyla- . rl 254 INDIAN 1. CHEM. TECHNOL., cetate obtained from a local industry, were recorded. Gas chromatographic analysis of all the products and authentic samples of isoamyl alcohol, acetic acid and ester were carried out using Netal Chromatograph (with a TCD and 2 m stainless steel column packed with DC-20() as the stationary phase) at a column temperature of 200°C using hydrogen as the carrier gas. Results and Discussion Gas chromatographic analysis clearly indicated that the zeolites showed 100% selectivity towards formation of the ester. The percentage of ester (as calculated from GC analysis) present in the product extract obtained from each of the reactions is given in Table 1. The effect of refluxing time and the amount of catalyst in the reaction in presence of HY is given in Table 2. IR spectra of some of the product samples (1, 2, 5, 9) mentioned in Table 1 are given in Fig. 1. Assignment of various absorption peaks! I in IR and IH NMR spectra indicate that the product is isoamyl acetate. It can be inferred from results (Table 1) that both Lewis acids and the zeolites catalyse esterification reaction and the catalytic activity of the zeolites used is comparable with that of concentrated sulphuric Table I-Catalytic activity of different Lewis acids and zeolites in esterif\cation reaction . Weight of the catalyst = 2g,Refluxingtime = 20h, Reaction mixture = 1:1 isoamyl alcohol and glacial acetic acid (1:1 molar). NaX HY NaZSM-579.00 HZSM-5 NaY HX 79.80 76.80 75.12 82.22 100.00 % of 78.87 75.62 ester in the 66.36 AICI] Catalyst ZnCI2 Sample number H2SO4 prod uct extract SEJYfEMBER 1996 acid. HZSM-5 being catalytically most active, showed 100% ester in the reaction product. NaX and NaY were found to have same activity as their protonated forms (HX and HY) under similar reaction conditions. When HY catalyst was employed, it was found that the yield of ester decreased with increase in retluxing time and decrease in the amount of catalyst (Table 2). Zeolites are known for their catalytic activity in a number of acid catalysed organic "reactions4. The strength and the distribution of the acid sites depend on the type of zeolitel2.This property of zeolites is clearly revealed in this investigation as different zeolites showed catalytic activity to different extents and it is not only the amount but also the strength of the acid sites associated with the zeolites that plays an important role in catalysing a particular reaction13·14. This property is observed in the present investigation in the case of NaX and NaY zeolites which showed almost same catalytic activity in terms of the per.centage of the ester formed, as their protonated forms, though the latter forms are known to have higher total acidity than their sodium forms. This is probably because the number and strength of acid sites responsible for catalytic activity remain almost the same in both sodium and protonated forms. Decrease in percentage of ester in the product extract when amount of the catalyst was decreased from 2 g to 1 g may be due to the decrease in the number of acid sites available for the reaction. The availability of the catalytic sites with appropriate acid strength in zeolites accounts for their higher catalytic activity on being compared with conventional Lewis acids. Conclusion In general, zeolites showed better catalytic aca b Table 2-Effect of reaction conditions on esterification activity of HY catalyst Reaction mixture-isoamyl alcohol and glacial acetic acid (I: I molar) hAmount ester 93.48 79.80 20 32 %ofthe 47.90 Refluxing time Catalyst I 3 S e "" E •• c: + d 13 •.. •.... 4000 35003-000- 2500 2000 l500 1000 500 Wavp numbprs ,em-I Fig. I-IR spectra of the product extracts obtained in the presence of (a) cone. H2S04, (b) HX, (c) ZnClz, (d) HZSM-5 catalysts, and (e) authentic sample isoamyl acetate I " I NAGARAJU & MEHBOOB: CATALYTIC ACTIVITY OF ZEOLITES tivity in the esterification reaction between isoamyl alcohol and acetic acid than the conventional Lewis acids such as anhydrous ZnCI2, AlCl) and cone. H2S04, The selectivity towards ester formation is 100%. Thus zeolites may be tailored to get active catalytic sites with appropriate acid strength to increase the percentage of ester in the reaction. Acknowledgements The authors acknowledge the assistance provided by Ms Joyce D'Souza and Ms Bina V in conducting some of the experiments. One of the authors (NN) is indebted to Dr A B Halgeri, IPCL, Baroda for his suggestions and constant encouragement. References 1 Fessenden R J & Fessenden J S, Organic chemistry (Brooks/Cole, California), 3rd ed, 1986,645. 2 Huai bin Z, Bao zen Z & He xuan L, Nat Gas Chem, 1 (1992) 49. 255 3 Tanabe K, Svlid adds & bases (Academic Press, New York), 1970. 4 Venito P B. Microporous Mater. 2 ( 1994) 297. 5 Richard W. MiCabe, in Inorganic Materials, edited by Bruce D Wand O'Hare D (John Wiley & Sons), 1992, 296. 6 PerotG&GuisnetM,JMoICatal,61 (1990) 173. 7 Xiu zhen L, Su jan L. Bai ying Z & Yi xiang Y, J Nat (jas Chem, 4 (1992) 375. 8 Hoefnagel A J & Bekkum H V, Appl Catal A, General, 97(1993)87. 9 Chern Zitao, Junshi Z, Quifang L, Yanhong L. Zhaohua 0& Zi Tao C, Sci China (Ser B), 32 (19H9) 769. 10 Furniss B S, Hannaford A J, Roger S Y, Smith P W G & TaTchell A R. in Vogels text book of practical organic chemistry, 4th edn (ELBS), P 501 and 1074. II Silverstein R M, Bassler G C & Morrill T C, Spectroscojr ic Identification of Organic Compounds (John Wiley & Sons, New York). 12 Dwyer J, in Zeolites microporous solids synthesis structure and reactivity, edited by Derouane E G, Lemos F, Naccache C and Ribeiro F (NATO, ASI Series, Kluwer, Dordrecht, 362 (1992) 303. 13 Corma A, Stud surfSci Catal, 52 (1989) 1. 14 Gao Oz & Tang Y, Acta Chem Sc~ 48 (1990) 638.
© Copyright 2025 Paperzz