CROWN ETHER(PHASE TRANSFER CATALYST) CONCENTRATION EFFECT ON KINETICS AND PRODUCT YIELD IN THE REACTION BETWEEN SOLID POTASSIUM

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ISSN: 0974-1496 e-issn: 0976-0083 CODEN: RJCABP http://www.rasayanjournal.com http://www.rasayanjournal.co.in CROWN ETHER(PHASE TRANSFER CATALYST) CONCENTRATION EFFECT ON KINETICS AND PRODUCT YIELD IN THE REACTION BETWEEN SOLID POTASSIUM p-nitrobenzoate AND BENZYL BROMIDE Sunil Kumar 1,* and Bigan Ram 2 1 Department of chemistry, L.N Mithila University, Kameshwarnagar, Darbhanga-846004, Bihar (India) 2 Department of Chemistry, Women s College, Samastipur-848101, Bihar (India) *E-mail:delhi2014india@gmail.com ABSTRACT 18-Crown-6 and other substituted 18-crown-6 ether used to change kinetics and product yield.in solid liquid phase transfer reaction in between solid potassium p-nitrobenzoate and benzyl bromide in chloroform, Percentage product yield variation observed due to different electron donating group in Crown ether.in most of the cases concentration of crown ether catalyst is directly proportional to reaction rate and % product yield.the reaction completed by nucleophilic substitution reaction mechanism. Keywords: Crown ether, Lipophilicity, Electron donating group, Heterogeneousprocess, Nucleophilic substitution, Complex formation constants and Interionic ion- pair distance. RASĀYAN. All rights reserved INTRODUCTION Crown ethers have been at the center of immense scientific and technological interest. This has been motive by the fascinating features of these macromolecules which mimic at the simplest level the action of the true enzymatic systems. Specifically, crown ethers can serve as active carries and the last can catalyzes reactions on bound substrates.the efficiency of Crown ethers as phase transfer catalyst depends on their complex cation constant with the reaction ion pairs,their ability to enlarge the interionic pair distance and the lipophilicity of the ion pair complexes.in general, the PTC reaction describes a methodology for accelerating the reaction between ionic compounds and organic, water-insoluble substance in solvents of low polarity. In this solid liquid phase transfer reaction between potassium p- nitrobenzoate and benzyl bromide 18 Crown 6,MB18C6,DH18C6 and B15C5 are used as phase transfer catalyst. The main aim of this experiment to observed variation of reaction rate and product yield when substituent of Crown ether changed. EXPERIMENTAL In a typical experiment chloroform (8ml) containing crown ether, 0.08 mmol and KNB 1.2 mmol was placed in a flask kept at 25±0.5ºC. After was stirring for 15 min,2.5 M Benzyl bromide was added. At intervals, depending on the reaction rate, a sample (50µl) of the clear chloroform solution was withdrawn and immediately diluted with chloroform solution(10 ml) to quench the reaction.the Benzyl p- nitrobenzoate product was determined quantitatively by HPLC. The reaction was usually monitored up to about 15% conversion. RESULTS AND DISCUSSION In this solid liquid phase transfer system, potassium p- nitrobenzoate is transferred to chloroform by means of the crown ether and the soluble crown ether potassium p-nitro benzoate complex(cr-knb) is converted into p- nitro benzoate (BzNB) by treatment with benzyl bromide..the mechanism of this heterogeneous process is depicted in Scheme-1 and equations 1 to 3. Rasayan J. Chem., 10(3), 929-934(2017) http://dx.doi.org/10.7324/rjc.2017.1031790

Scheme-1:The Reaction between solid Potassium p-nitrobenzoate and Benzyl bromide in chloroform CR ORg + KNBsolid CR-KNB org (1) CR-KNBorg+ PhCH2Br org PhCH2NBorg + CR KBr org (2) CR KBr orgcr org + KBRsolid (3) The following assumptions are made: 1. The phase transfer process (1) and (3) are much faster than the nucleophilic substitution reaction (2). 2. The concentration of the CR-KNB complex depends only on the initial crown ether concentration in the organic phase. 3. Crown ether complexation to KNB is appreciably greater than to KBr is appreciable, implying that the concentration of the CR-KNB remains essentially constant during the reaction.the rate of product formation is given by Equation-4, where K obsis the pseudo- first order rate constant.integration yields equation-5.depending on reaction conditions, benzyl bromide can undergo either SN 1 and SN 2 reactions; hence the rate of product formation can be expressed as Equation-6, combining (4) and (6) yields equation-7 and thus K 1 and K 2 can be obtained by measuring K obs as a function of the Crown ether-salt complex concentration. d[phch 2NB]/dt = K[PhCH 2Br] [CR-KNB] = Kobs[PhCH2Br] (4) -In[PhCH 2Br] o - [PhCH 2NB] = Kobs + -In[PhCH 2Br] o (5) d [PhCH 2NB]dt = K 1 [PhCH 2Br]+K 2[PhCH 2Br] [CR-KNB] = {K 1+K 2[CR-KNB] }[PhCH 2Br] (6) Kobs = K 1+K 2 [CR-KNB] (7) Phase transfer equilibrium and extent of salt transfer using conditions similar to those employed in the kinetic studies.it was found that phase transfer equilibrium can be attained within 2 min. Figure-1 shows plots of UV absorbance versus time for transfer of KNB to chloroform containing Oxydimethylenebisbenzo-15-crown-5 and dicyclohexano-18-crown-6. The time needed to reach equilibrium is not affected by the rate of stirring or a change in particle size from 100 to 150 mesh but the 930

use of non-ground KNB increases the equilibration time to 5 min. These results justify the previously made assumption that the phase transfer step is much faster than ester formation, the half-life of which lie between10 2 and 10 3 min,depending on the crown ether used The function [CR-KNB]/ [CR] o can be used as a measure of the efficiency of a crown ether in transferring the solid KNB salt transferred into the organic phase.no detectable amount of salt is transferred in the absence of crown ether, but Table-1 shows that the above function reaches 0.95 for 18C6,MB18C6 and DH18C6 and 1.0 for bis B15C5, implying that nearly every crown ether molecule in the CHCl 3 solution is bound to a K + ion. At 25ºC a complex concentration of 0.06 M in CHCl 3 can be easily attained. Since KBr is a reaction product it conceivably could compete with KNB for crown ether and consequently lower the CR-KNB concentration during the reaction. However, during the reaction, the concentration of CR-KNB was found to be constant up to at least 20% conversion of PhCH 2Br.Also, addition of solid KBr in an amount equal to that produced after 20% conversion has no effect on the concentration of CR-KNB.Apparently, the reaction product CR-KBr decomposes into solid KBr and free crown ether, the latter solubilizing solid KNB to maintain a constant CR-KBN concentration. The different behavior of KBr and KNB depends on such factors as the crystal lattice energy of the salt and the complex formation constants of the crown ether with the two salts. Plots of In[PhCH 2Br] o - [PhCH 2NB] versus reaction time for bis B15C5-catalyzed reaction of solid KNB with PhCH 2Br at various crown ether concentrations are shown in Fig.-2. The observed pseudo first order rate constants,k obs calculated from the least squares straight lines are listed in Table-3 together with other reaction variables. It was ascertained that no reaction occurs in the absence of Crown ether. Figure-3 depicts plots of Kobs versus the complexed salt concentration (Cr-KNB).All crown ethers show linear relations with intercepts very close to zero. The intercepts, representing K1 for benzyl bromide in CHCl 3 at 25 o C(equation-7), are less than 10-6 min -1.Small SN 1 rate constants are expected since in a low polarity solvent such as chloroform the SN 1 pathway is insignificant. The same reaction gave K1=10-5 min -1 in the more polar solvent dichloromethane. Fig.-1: Plots of the absorbance of the crown ether-potassium p-nitrobenzoate complex versus stirring time in solid CHCl 3 phase-transfer process at 25 o C: A,[bisB15C5]=5.0x10-3M at ʎ max.280;[dh18c6]=5.0x10-3 M at ʎ max 272 nm; cell length=1.0 cm(the sample was diluted 200 times before UV measurement) The SN 2 rate constants calculated from the slopes the plot of Fig.-3is listed in Table -2.The K2 values in the presence of 18Crown6, MB18 C6,DH18C6 differ by not more than a factor of 1.5, but the K2 values in the presence of bis B15C5 are about ten times larger. The much higher K2 value with bis B15C5 is most likely caused by the larger CO 2- ---K + interionic distance in its complex with the bis-crown ether.at the concentrations employed in these studies, the 931

crown ether-salt complex in CHCl 3 is undoubtedly an ion pair.moreover,the concentration of the crown ether-ion pair complex indicates that the reaction proceeds via the ion pairs and that no reactive free ions are involved.studies have shown that the interionic ion- pair distance in a crown ether ion pair complex is sensitive to the structure of the crown ether and the types of cation and anion composing the ion pair. In systems where 1:1 crown ether-cation complexes tight ions pairs are frequently observed in less polar media like CHCl 3 or diethyl ether,especially for less delocalized anions.the interionic ion pair distance in the complexes appears to increase in the order 18C6~MB18C6<DH18C6<<bisB15C5. This change corresponds with the increase in K2 found for these crown ether (Fig.-2 and 3). Fig.-2:Plots of ln[phch 2Br] o-[phch 2NB] versus reaction time for the solid CHCl 3 phase transfer reaction between potassium p-nitrobenzoate and benzyl bromide catalysed by oxymethylenebisbenzo-15-crown-5 at 25 o C : a,[cr] o=1.3x10-3 M; b, [CR] o=3.0 x10-3 M; c,[cr] o=5.0x10-3 M; d,[cr] o=1.2x10-2 M; e,[cr] o=1.5x10-2 M. Table-1: Efficiency of transfer of solid potassium p-nitrobenzoate into chloroform by crown ethers at 25 o C S. No. Name of crown ether Fraction of crown ether complexed to crown ether Concentration range of crown ether10 2 [Cr] o/m 01 18-Crown-6 0.95 0.50-5.0 02 4-Methylbenzo18-Crown-6 0.95 0.60-5.0 03 Dicyclohexano 18-Crown-6 0.95 0.5-6.0 04 Oxymethylenebisbenzo 15- Crown-5 1.0 0.13-2.3 Table-2: Second order rate constants (K 2) for the reaction between potassium p-nitrobenzoate and benzyl bromide catalyzed by crown ethers in CHCl 3 at 25 O C S.No. Name of crown 10 2 k 2/1 mol -1 min -1 Range of crown ether concentration(10 2 [CR]/M) ether 01 18C6 1.30 0.50-5.00 02 MB18C6 1.13 0.60-5.00 03 DH18C6 1.84 0.50-6.00 04 BisB15C5 9.66 0.13-2.25 05 Mb15C5 0.14 1.00-7.00 932

Fig.-3:Plots of Kobs versus[ CR-KNB] in the solid CHCl 3 phase transfer reactions catalysed by various crown ethers at 25 o C:A,18C6,B MB18C6,C,DH18C6,D,BISB15C5. Table-3: Pseudo-first-order rate constants,k obs for the reaction between potassium p-nitrobenzoate and benzyl bromide in a solid-chcl 3 phase transfer system catalyzed by various crown ethers at 25 o C Crown ether 18C6 MB18C6 DH18C6 Bis B15C5 10 2 [CR] o M [PhCh 2Br] o M Wt,KNB g 10 2 [CR-KNB] o M 10 4 K obs MIN -1 Conversion (%) 0.48 0.481 0.15 0.46 0.69 0.9 1.00 0.506 0.15 0.95 1.24 4.5 3.00 0.253 0.10 2.85 3.63 5.7 5.00 0.252 0.20 4.75 6.17 6.0 1.00 0.503 0.20 0.95 0.98 3.6 2.00 0.503 0.20 1.92 1.92 6.3 3.00 0.503 0.25 2.88 3.09 9.7 4.00 0.503 0.25 3.80 4.72 11.0 0.50 0.500 0.25 0.48 1.08 3.8 1.00 0.500 0.25 0.95 2.19 10.8 2.00 0.500 0.25 1.90 4.25 16.4 2.52 0.490 1.00 2.39 5.23 15.0 3.50 0.500 0.25 3.80 6.87 10.6 4.00 9.500 0.25 3.80 7.45 7.6 4.50 0.500 0.25 4.28 8.49 10.9 5.00 0.500 0.25 4.75 9.83 16.8 6.00 0.500 0.25 5.70 10.8 17.0 0.13 0.501 0.25 0.13 1.16 4.8 0.30 0.501 0.25 0.30 2.85 10.1 0.50 0.501 0.25 0.50 5.38 7.5 0.80 0.501 0.25 0.80 7.28 5.0 1.20 0.501 0.25 1.20 11.1 5.5 1.35 0.501 0.25 1.35 13.5 9.5 1.50 0.501 0.25 1.50 15.8 10.4 1.80 0.501 0.25 1.80 17.5 8.3 2.20 0.248 0.25 2.25 20.4 9.6 933

CONCLUSION In conclusion, we have demonstrated a method for the synthesis of Benzyl p-nitrobenzoate from potassium p-nitrobenzoate and benzyl bromide in chloroform by using Crown ether phase transfer catalyst.the yields are quite good and the reactions are faster. The concentration of crown ether catalyst is directly proportional to rate constant and product yield. When different electron donating group used in Crown ether, the variation observed in rate constant and product yield. It is found that the presence of more electron donating group increases the reaction rate and product yield. ACKNOWLEDGEMENT One of the authors (Sunil Kumar) is thankful to Prof. I. S Jha and Prof. S. Jha, Department of Chemistry, L.N. Mithila University, Darbhanga for providing valuable suggestions and constant support to carry out present Research work. REFERENCES 1. Sanjeev D. Naik and L.K. Doraiswamy, Chemical Engineering Science, 52(24),4533( 1997) 2. Ganapat D. Yadav and Man Mohan Sharma, Ind. Eng. Chem. Process Des. Dev., (20), 385(1981) 3. Kam-Han Wong and Alex P. W. Wai, Journal of the Chemical Society, Perkin Transactions, 2(3)213(1983) 4. Sergio. Alunni, Enrico. Baciocchi and Piero. Perucci, J. Org. Chem., 41 (15),2636( 1976) 5. Angela K. Dillow, S. L. Jimmy Yun, David Suleiman, David L. Boatright, Charles L. Liotta, and Charles A. Eckert, Ind. Eng. Chem. Res, 35 (6), 1801(1996) 6. Hayder A. Zahalka,Yoel Sassonand Oel Sasson., Can. J. Chem., 67, 245 (1989) 7. Arthur W. Herriott and Donald Picker. J. Am. Chem. Soc, 97 (9), 2345( 1975) 8. I. A. Esikova, and S. S. Yufit, Physical Organic Chemistry, 4(3), 149,157 ( 1991) [RJC-1790/2017] 934