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Original article
10 (
2_suppl
); S2742-S2749
doi:
10.1016/j.arabjc.2013.10.020

Quantitative correlation between counterion (X) binding affinity to cationic micelles and X – Induced micellar growth for substituted iodobenzoates (X)

Department of Chemistry, Faculty of Science, University of Malaya, 50603 Kuala Lumpur, Malaysia

⁎Corresponding author. Tel.: +60 3 7967 4163; fax: +60 3 7967 4193. niyaz@um.edu.my (M. Niyaz Khan)

Disclaimer:
This article was originally published by Elsevier and was migrated to Scientific Scholar after the change of Publisher.

Peer review under responsibility of King Saud University.

Abstract

A new semi-empirical kinetic (SEK) method has been used to calculate the values of K X Br or R X Br (X represents substituted iodobenzoates), with KX and KBr representing CTABr micellar binding constants of counterions X (in the presence of either spherical or non-spherical micelles) and Br (in the presence of only spherical micelles), respectively. Steady-shear rheological properties of mixed 0.015 M CTABr/[MX] aqueous solutions reveal the presence of flexible wormlike micelles where MX represents sodium 3- and 4-iodobenzoates. The maxima of the plots of viscosity vs. [MX] at 0.015 M CTABr for MX representing sodium 3- and 4-iodobenzoates support the presence of long linear and entangled wormlike micelles.

Keywords

Rheometric measurements
Counterion micellar binding
Substituted iodobenzoates
Kinetics
Piperidine
Phenyl salicylate
1

1 Introduction

A recent review (Jungwirth and Tobias, 2006) highlights that specific ion effects on aqueous interfaces are ubiquitous both in physical and chemical processes occurring in almost all branches of life and apparent non-life sciences. Kunz et al. (2004) have pointed out that although Hofmeister effects, also known as specific ion effects, are universal in biology (Thirumalai et al., 2012), biochemistry (Berkowitz and Vacha, 2012) and chemical engineering, for over a hundred years, Hofmeister effects have not been encompassed by theories of solution or colloid chemistry. Similarly, Romsted (2007) has pointed out that the forces contributing to specific ion effects are difficult to identify, both experimentally and theoretically.

It has been known for the last nearly 4 decades that the structural features of counterions play a crucial and important role in the ionic micellar structural transition from spherical to threadlike to flexible entangled wormlike micelles (Magid, 1998; Abdel-Rahem, 2008; Rao et al., 1987; Lin et al., 1994). Qualitative experimental observations on ionic micellar headgroup interaction with counterions (X) show that strong ionic micellar binding of counterions results in such micellar structural transition (Lu et al., 1998; Bijma and Engberts, 1997; Ali et al., 2009). Even the recent such studies lacked the quantification of X affinity to ionic micelles and consequently a quantitative correlation between X affinity to micelles and X-induced micellar growth could not be found in these studies (Ketner et al., 2007; Lin et al., 2009a,b; Sreejith et al., 2011). The competitive binding affinities of X to ionic micelles have been studied because of their importance in the kinetic data analysis of ionic micellar-mediated semi-ionic bimolecular reactions (Bunton, 2006), industrial processes (Qi and Zakin, 2002) and separation science (Trone et al., 2000).

The quantification of counterion (X) binding efficiency with ionic micelles may be achieved in terms of the magnitudes of either the degree of counterion binding (βX) or usual ion exchange constant ( K X Br ) or R X Br with R X Br  = KX/KBr where the values of cationic micellar binding constants KBr and KX have been derived from the physicochemical parameters obtained in the presence of spherical and non-spherical micelles, respectively (Khan, 2006). However, the values of βX for X representing benzoate ions (Wang et al., 2010) as well as 2-, 3- and 4-CH3Bz (where Bz = C6H4CO2) of cationic micelles are nearly same (Vermathen et al., 2002) but their effects on cationic micellar growth are not the same (Rehage and Hoffmann, 1991). The reported values of K X Br or R X Br for X = 3- and 4-CH3Bz are nearly 3-fold larger than that for 2-CH3Bz (Khan and Kun, 2001; Khan and Ismail, 2007). In view of these reports, the values of K X Br or R X Br seem to correlate better than those of βX with X-induced micellar structural growth for different moderately hydrophobic X. But, it is not easy to determine accurately K X Br because the magnitudes of K X Br are very much technique-dependent (Magid et al., 1997; Romsted, 1984). A search of the literature reveals a very limited number of the reported values of ion exchange constants with X representing moderately hydrophobic counterions, obtained in the presence of cationic micelles (Magid et al., 1997; Gamboa et al., 1989; Bachofer and Simonis, 1996). A new semi-empirical kinetic (SEK) method has been used to determine the values of K X Br or R X Br for X representing both moderately hydrophilic and hydrophobic counterions (Khan, 2006). The effects of the inert counterionic salts on the rates of some ionic micellar-mediated reactions have been quantitatively explained in terms of pseudophase ion exchange (PIE) model (Romsted, 1984). The chemical trapping method of Romsted has been used to determine the value of KXCl as 2.6 for X = Br (Romsted, 2007) which is similar to ones determined by various methods including the SEK method (Khan and Sinasamy, 2011).

A search of the literature reveals that the values of K X Br or R X Br for X = 2-, 3- and 4-IBz are unknown. In the continuation of our study (Yusof and Khan, 2010, 2011) on the use of the SEK method for the determination of K X Br or R X Br for various X, the present manuscript reports the results for X = 2-, 3- and 4-IBz. The aims of the present study were (i) to determine the values of K X Br or R X Br for MX = 2-, 3- and 4-IBzNa at different total concentrations of CTABr, (ii) to carry out the rheometric measurements on mixed aqueous solutions of CTABr and MX (MX = 2-, 3- and 4-IBzNa) and (iii) to discover a possible quantitative correlation between the values of K X Br or R X Br and X-induced micellar growth. The quantitative correlation between the values of K X Br or R X Br and X-induced micellar growth has a predictive strength in the sense that the values of K X Br or R X Br can predict whether the X-induced micellar structure is spherical, rodlike/wormlike micelles or even unilamellar vesicles at a constant concentration of CTABr within its range 0.005–0.015 M. The observed results and their probable explanations are described in this manuscript.

2

2 Experimental

2.1

2.1 Materials

Chemicals such as cetyltrimethylammonium bromide (CTABr; purity ⩾99% from Fluka), phenyl salicylate (PSaH; purity ⩾98% from Fluka), piperidine (Pip; purity ⩾99% from Merck), 2-, 3- and 4-IBzH with BzH representing C6H4CO2H (2-IBzH; purity ⩾99% from Merck, 3-IBzH; purity 98% from Aldrich and 4-IBzH; purity ⩾98% from Merck) and NaOH (purity ⩾99% from Merck) were commercial products with highest available purity. The details of the preparation of the stock solutions of organic salts (MX = 2-, 3- and 4-IBzNa) and PSaH were the same as described earlier (Yusof and Khan, 2011). Because of the extremely low water solubility of PSaH, the stock solutions (0.01 M) of PSaH were prepared in pure acetonitrile.

2.2

2.2 Kinetic measurements

The rate of reaction between piperidine (Pip) and ionized phenyl salicylate (PSa) was studied spectrophotometrically by monitoring the disappearance of PSa as a function of reaction time (t) at a constant wavelength of 350 nm by using UV-visible spectrophotometer equipped with electronically controlled thermostatic cell compartment set at 35 °C. The details of the kinetic procedure and product characterization study were the same as described elsewhere (Khan and Kun, 2001). Nonlinear least-squares technique was used to calculate kinetic parameters kobs (pseudo first-order rate constant), δap (apparent molar absorptivity of the reaction mixture) and A (absorbance at t = ∞) from Eq. (1) (Khan and Kun 2001).

(1)
A ob = [ R 0 ] δ ap exp ( - k obs t ) + A where Aob is the absorbance at any reaction time (t) and [R0] is the initial concentration of PSaH. Almost all the kinetic runs were carried out for the reaction period equivalent to ∼9 half lives of the reaction.

2.3

2.3 Rheometric measurements

The rheological study was carried out using a Brookfield R/S+ rheometer with double gap coaxial cylinder (CC–DG) and an external temperature controller fixed at 35 °C. The concentrations of all additives except CTABr of a rheological sample were same as maintained in the kinetic measurements. The concentration of CTABr was kept constant at 0.015 M. The sample was thermally equilibrated at 35 °C for at least 15 minutes. The shear rate ( γ ̇ ) range was fixed at 0.5–15 s−1 and 1–1000 s−1 for respectively the total time of 2400 s and 8000 s, for the rheological measurements. The total number of data points was 30 for the first set and 100 for the second set.

2.4

2.4 Determination of K X Br or R X Br for X = 2-, 3- and 4-IBz by the use of SEK method

The semi-empirical kinetic (SEK) method for the determination of K X Br or R X Br requires the use of a reaction kinetic probe which involves the kinetic study on the effects of the concentrations of the inert salts of counterions (such as [MX] where MX = 2-, 3- and 4-IBzNa) on kobs for the cationic micelle-catalyzed semi-ionic bimolecular reaction with the ionic reactant representing as the counterion of cationic micelle. The reaction kinetic probe that has been used in the present study, involves the nucleophilic reaction of Pip with PSa. The details of the SEK method including the reaction kinetic probe used in the present study are described in a recent report (Yusof and Khan, 2010; Khan, 2010).

3

3 Results

3.1

3.1 Effects of the concentrations of 2-, 3- and 4-IBzNa (Bz = C6H4CO2) on the rate of piperidinolysis of PSa at a constant [CTABr]T and 35 °C

Several kinetic runs were carried out at different concentrations of MX (= 2-, 3- and 4-IBzNa) within [MX] range 0.0 – ⩽0.30 M at 0.005 M CTABr, 0.1 M Pip and 2 × 10−4 M PSa. The values of [NaOH], under such conditions, varied from 0.03 to 0.06 M for 2-IBzNa and 0.03 to 0.04 M for 3- and 4-IBzNa. The values of pseudo-first-order rate constants (kobs), at different [MX] are shown graphically in Fig. 1 for MX = 3-IBzNa and Figs. S1 and S2 of Supplementary Data (SD) for respective MX = 2 and 4-IBzNa. Similar observations were obtained at 0.006, 0.007, 0.01 and 0.015 M CTABr for MX = 2-IBzNa while for 3- and 4-IBzNa, the observed data could be obtained only at ⩽0.01 M CTABr. The values of kobs at different [MX] and at a constant 0.015 M CTABr, for MX = 3- and 4-IBzNa could not be obtained because the reaction mixture, even at the lowest value of [MX] (= 0.002 M), became jelly at the reaction time t = 0. As a consequence, the reaction mixtures under such conditions became highly viscous and inhomogeneous as well as observed data, Aob vs. t, did not fit to Eq. (1). The values of kobs at different [MX] and [CTABr]T are also shown graphically in Fig. 1, S1 and S2 for MX = 3-, 2- and 4-IBzNa, respectively.

Plots showing the dependence of kobs upon [MX] (MX = 3-IBzNa) for piperidinolysis of PSa− at 2 × 10−4 M PSa−, 0.1 M Pip, ⩽0.06 to >0.03 M NaOH, 35 °C and [CTABr]T/M = 0.002 (●), 0.005 (▴), 0.006 (■), 0.007 (○) and 0.01 (Δ). The dashed lines are drawn through the calculated data points using Eq. (2) with kinetic parameters (k0, θ and KX/S), listed in Table 1 of manuscript, at [MX]0op = 0. The solid lines are drawn through the calculated data points using Eq. (2) with kinetic parameters (k0, θ and KX/S), listed in Table 1 of manuscript, at [MX]0op/M = 0.0044 (●), 0.0045 (▴), 0.0046 (■), 0.0050 (○) and 0.0094 (Δ). Inset: The plots at magnified scale for the data points at the lowest values of [MX].
Figure 1
Plots showing the dependence of kobs upon [MX] (MX = 3-IBzNa) for piperidinolysis of PSa at 2 × 10−4 M PSa, 0.1 M Pip, ⩽0.06 to >0.03 M NaOH, 35 °C and [CTABr]T/M = 0.002 (●), 0.005 (▴), 0.006 (■), 0.007 (○) and 0.01 (Δ). The dashed lines are drawn through the calculated data points using Eq. (2) with kinetic parameters (k0, θ and KX/S), listed in Table 1 of manuscript, at [MX]0op = 0. The solid lines are drawn through the calculated data points using Eq. (2) with kinetic parameters (k0, θ and KX/S), listed in Table 1 of manuscript, at [MX]0op/M = 0.0044 (●), 0.0045 (▴), 0.0046 (■), 0.0050 (○) and 0.0094 (Δ). Inset: The plots at magnified scale for the data points at the lowest values of [MX].

3.2

3.2 Effects of [MX] (MX = 2-, 3- and 4-IBzNa) on kobs for the reaction of Pip with PSa in the absence of CTABr at 35 °C

Although benzoate and substituted benzoate ions are nonreactive toward nucleophilic cleavage of PSa, these inert salts might affect rate of piperidinolysis of PSa through specific salt/ionic strength effect. In order to find out this probable salt effect on kobs, a few kinetic runs were carried out at 0.1 M Pip, 2 × 10−4 M PSa and within [MX] (MX = 2-, 3- and 4-IBzNa) range 0.0–0.3 M in the absence of CTABr. The values of [NaOH] varied within its range 0.03–0.06 M. The least-squares calculated values of kinetic parameters, kobs and δap reveal that the values of kobs are almost independent of [MX] within its range 0.0–0.2 M for MX = 2-IBzNa, 0.0 – 0.10 M for MX = 3- and 4-IBzNa. Mean values of kobs (i.e., kobsmean) are (316 ± 13) × 10−4, (323 ± 10) × 10−4 and (311 ± 14) × 10−4 s−1 for MX = 2-, 3- and 4-IBzNa, respectively. The value of kobs at 0.3 M 2-IBzNa is ∼10% lower than the mean value of kobs (= (316 ± 13)) × 10−4 s−1). The values of δap remain independent of [MX] within its range 0.0 – 0.3 M and mean values of δap (i.e., δapmean) are 6866 ± 106, 6769 ± 107 and 6871 ± 178 M−1 cm−1 for MX = 2-, 3- and 4-IBzNa, respectively.

3.3

3.3 Rheological properties of CTABr micellar solutions containing constant concentrations of PSa, Pip, MX and >0.03 to ⩽0.04 M NaOH

Rheological behaviors of CTABr/2-IBzNa, CTABr/3-IBzNa and CTABr/4-IBzNa were studied at 33.9 ± 1.6 °C under steady-shear rheological response. Aqueous surfactant (CTABr) solutions containing 2% v/v CH3CN and a constant concentration of all additives (2 × 10−4 M PSa, 0.1 M Pip, ⩽0.06 M NaOH) including 0.015 M CTABr as well as different concentrations of MX (= 2-, 3- and 4-IBzNa) were used to obtain shear viscosity (η) at different shear rates ( γ ̇ ) within its range >0.4 – 1000 s−1. The log–log plots of η vs. γ ̇ at different values of [MX] are shown graphically by Fig. 2 for MX = 3-IBzNa and respective Figs. S3 and S4 of (SD) for MX = 2- and 4-IBzNa. Similar observations were also obtained at 0.005 M CTABr for 4-IBzNa simply for comparison purpose because the values of η, at shear rates 10 and 1000 s−1 and within [4-IBzNa] range 0.003 – 0.02 M at 0.005 M CTACl and 30 °C, are available from a recent report (Ge et al., 2008). The values of η vs. γ ̇ are shown graphically as log–log plots in Fig. S5. The plots of Fig. 2 and Figs. S3–S5 represent shear thinning which is a typical characteristic of the presence of rodlike micelles (RM)/wormlike micelles (WM) in the surfactant solutions (Lin et al., 2009a; Lin et al., 2009a; Lu et al., 2008; Raghavan and Kaler, 2001).

Plots showing the dependence of shear viscosity (η) upon shear rate ( γ ̇ ) for samples where [PSaH] = 2 × 10−4 M, [NaOH] = 0.03 M, [Pip] = 0.1 M, [CTABr] = 0.015 M and [3-IBzNa]/M = 0.01 (Δ), 0.03 (▴), 0.05 (■) and 0.1 (□).
Figure 2
Plots showing the dependence of shear viscosity (η) upon shear rate ( γ ̇ ) for samples where [PSaH] = 2 × 10−4 M, [NaOH] = 0.03 M, [Pip] = 0.1 M, [CTABr] = 0.015 M and [3-IBzNa]/M = 0.01 (Δ), 0.03 (▴), 0.05 (■) and 0.1 (□).

The values of η at γ ̇ = 2.5 s - 1 , i.e. η 2.5 γ ̇ , 0.015 M CTABr and different [MX] are shown graphically in Fig. 3 for MX = 2-, 3- and 4-IBzNa. The plot of η 2.0 γ ̇ vs. [4-IBzNa] at 0.005 M CTABr is also shown in Fig. 3. A remarkable rheological feature of adding salt (MX) to aqueous surfactant solutions is the maximum shown by the plot of η γ ̇ vs. [MX]. Although this behavior is no longer unusual for long wormlike micellar systems (Rehage and Hoffmann, 1991; Schubert et al., 2004; Croce et al., 2005; Ali and Makhloufi, 1997; Davies et al., 2006), the mechanism, at the molecular level for the occurrence of such maximum, is still a matter of debate (Davies et al., 2006; Dreiss, 2007).

Plot of shear viscosity (η) at γ ̇  = 2.5 s−1 vs. [MX] ([MX] = [2-IBzNa] (×), [3-IBzNa] (▴) and [4-IBzNa] (●)) at 0.015 M CTABr as well as the plot of η at γ ̇  = 2.0 s−1 vs. [MX] (MX = 4-IBzNa) (○) at 0.005 M CTABr, 2 × 10−4 M PSa−, 0.03 M NaOH and 0.1 M Pip and ∼35 °C.
Figure 3
Plot of shear viscosity (η) at γ ̇  = 2.5 s−1 vs. [MX] ([MX] = [2-IBzNa] (×), [3-IBzNa] (▴) and [4-IBzNa] (●)) at 0.015 M CTABr as well as the plot of η at γ ̇  = 2.0 s−1 vs. [MX] (MX = 4-IBzNa) (○) at 0.005 M CTABr, 2 × 10−4 M PSa, 0.03 M NaOH and 0.1 M Pip and ∼35 °C.

4

4 Discussion

4.1

4.1 Determination of K X Br or R X Br for X = 2-, 3- and 4-IBz

It is evident from Fig. 1 and Figs. S1 and S2 that the values of kobs are more than 10-fold smaller at [MX] = 0 and [CTABr]T ≠ 0 than those at [CTABr]T = 0, and at different [MX] within its range 0 – ⩽0.2 M. Thus, the nonlinear increase in kobs with the increasing values of [MX] at a constant [CTABr]T cannot be explained in terms of ionic strength effect. The most plausible cause for the nonlinear increase in kobs with the increase of [MX] is the transfer of micellized PSa (i.e., PSaM with subscript ‘M’ indicating micellar pseudophase) to the bulk water phase (i.e., PSaW with subscript ‘W’ indicating water phase) through the ion exchange process X/PSa. The values of kobs, at different [MX] (MX = 2-, 3- and 4-IBzNa) and at a constant [CTABr]T, were treated with Eq. (2) (Khan and Ismail, 2007; Khan, 2010).

(2)
k obs = k 0 + θ K x / s [ MX ] 1 + K x / s [ MX ] where θ and KX/S are empirical constants and k0 = kobs at [MX] = 0 as well as [Dn] ≠ 0 (where Dn represents micellized CTABr). The nonlinear least-squares technique was used to calculate θ and KX/S as well as least squares, Σdi2, (where di = kobs i – kcalc i with kobs i and kcalc i representing respective experimentally determined and least-squares calculated rate constants, at the i-th value of [MX]), from Eq. (2) by considering k0 as the known parameter determined experimentally at [MX] = 0. The calculated values of θ, KX/S and Σdi2 at different [CTABr]T for MX = 2-, 3- and 4-IBzNa are shown in Table 1.
Table 1 Values of the empirical constants θ and KX/S, calculated from Eq. (2) (where [MX] = [MX]Sef with zero and nonzero [MX]0op values) for different MX in CTABr micelles.a
[CTABr]Tb (mM) 104 koc (s−1) [MX]oop (mM) 104 θ (s−1) KX/S (M−1) KX/S (M−1) FX/S KX/Sn (M−1) R X Br 108 (∑di2)
MX = 2-IC6H4CO2Na
 5.0 29.3 4.5 254 ± 2.4d 9.78 ± 0.24d 352e 0.78f 275g 11.0h 13.21
 5.0 29.3 0 274 ± 12 7.56 ± 0.75 272 0.84 228 9.12 210.4
 6.0 28.8 5.6 261 ± 6.5 8.51 ± 0.52 366 0.80 293 11.8 66.11
 6.0 28.8 0 286 ± 16 6.39 ± 0.82 275 0.87 239 9.56 272.9
 7.0 27.9 7.8 246 ± 7.3 7.96 ± 0.57 398 0.75 299 12.0 62.90
 7.0 27.9 0 278 ± 22 5.49 ± 0.89 275 0.85 234 9.36 286.4
 10.0 27.1 9.7 229 ± 8 5.88 ± 0.45 417 0.70 292 11.7 38.30
 10.0 27.1 0 274 ± 32 3.72 ± 0.78 264 0.84 222 8.88 240.0
 15.0 26.2 14.0 220 ± 17 3.42 ± 0.44 363 0.67 243 9.72 9.651
 15.0 26.2 0 587 ± 533 0.79 ± 0.84 83.7 1.80 151 6.04 96.44
MX = 3-IC6H4CO2Na
 2.0 30.5 4.4 313 ± 1.4 247 ± 7.36 3705 0.96 3557 142.3 90.03
 2.0 30.5 0 344 ± 17 90.6 ± 19.2 1450 1.05 1523 60.9 611.57
 5.0 29.5 4.5 325 ± 3.3 112 ± 5.64 4032 0.99 3992 159.7 26.57
 5.0 29.5 0 368 ± 21 49.3 ± 9.61 1775 1.13 2006 80.2 463.8
 6.0 28.4 4.6 322 ± 3.9 93.1 ± 5.21 4003 0.98 3923 156.9 30.92
 6.0 28.4 0 371 ± 23 41.9 ± 8.45 1802 1.13 2036 81.4 451.25
 7.0 27.1 5.0 322 ± 5.9 72.5 ± 5.46 3625 0.98 3553 142.1 45.41
 7.0 27.1 0 367 ± 16 36.7 ± 5.00 1835 1.12 2055 82.2 151.2
 10 26.2 9.4 322 ± 6.0 48.1 ± 3.11 3415 0.98 3347 133.9 19.28
 10 26.2 0 433 ± 65 16.3 ± 5.26 1157 1.32 1527 61.1 394.7
MX = 4-IC6H4CO2Na
 5.0 30.9 4.4 293 ± 2.4 115 ± 4.0 4140 0.90 3726 149 72.38
 5.0 30.9 0 335 ± 25 51.2 ± 11 1843 1.02 1880 75.2 3452
 6.0 29.3 4.8 284 ± 5.0 105 ± 7.6 4515 0.87 3928 157 278.9
 6.0 29.3 0 333 ± 31 44.0 ± 12 1892 1.02 1930 77.2 4373
 7.0 27.2 5.5 289 ± 8.5 78.4 ± 8.3 3920 0.88 3450 138 500.0
 7.0 27.2 0 333 ± 30 37.3 ± 9.0 1865 1.02 1902 76.1 2746
 10.0 26.2 9.4 262 ± 0.2 56.1 ± 0.1 3983 0.80 3186 127 0.075
 10.0 26.2 0 361 ± 30 37.2 ± 9.0 2641 1.10 2905 116 2380
[MX] = 2-IBzNa, 3-IBzNa and 4-IBzNa.
Total concentration of CTABr.
k0 = kobs at [MX] = 0.
Error limits are standard deviations.
KX/S = KX/S (1 + KS0[CTABr]T) where KS0 = 7000 M−1.
FX/S = θ/kW where kW = kobs at [CTABr]T = 0, [Pip]T = 0.1 M and the value of kW, under such conditions, is 32.7 × 10−3 s−1 at 35 °C.
KX/Sn = FX/SKX/S.
R X Br  = KX/Sn/KBr/Sn, where KBr/Sn = 25 M−1.

The plots of Fig. 1 as well as Figs. S1 and S2, where dashed lines are drawn through the least squares calculated rate constants using Eq. (2) with kinetic parameters (θ and KX/S) listed in Table 1, reveal significant systematic negative deviations of the observed data points from dashed lines at the lower values of [MX]. The reason for these significant negative deviations of the observed data points from the corresponding calculated data points with the decreasing [MX] at its extreme lower values as well as higher values of [CTABr]T has been attributed to the significant effects of the ion exchange processes X/HO and X/Br on kobs under such typical reaction conditions (Khan and Ismail, 2007; Yusof and Khan, 2010; Khan, 2010). The consideration of these independent ion exchange processes has led to Eq. (3) (Khan and Ismail, 2007; Khan, 2010)

(3)
[ MX ] S ef = [ MX ] - [ MX ] 0 op where [MX]Sef represents the effective concentration of MX that could affect the ion exchange X/S (S = PSa) and [MX]0op is the optimum value of [MX] at which the value of ([HOM] + [BrM]) becomes independent of [MX]. The values of [MX]0op at different values of [CTABr]T were estimated by an iterative technique (Yusof and Khan, 2010; Khan, 2010). These calculated values of [MX]0op are summarized in Table 1. The values of θ, KX/S and Σdi2 were also calculated from Eq. (2) with [MX] = [MX]Sef and these results are also shown in Table 1. It is evident from the plots of Fig. 1 as well as Figs. S1 and S2, (where solid lines are drawn through the calculated data points using Eq. (2) and kinetic parameters, θ and KX/S), with [MX] = [MX]Sef as well as from the values of Σdi2 that the observed data treatment with Eq. (2) is more reliable with [MX] = [MX]Sef at [MX]0op ≠ 0 compared with that at [MX]0op = 0.

The effective occurrence of ion exchange process X/S in the related reaction systems has been found to decrease KS with the increasing [MX] through an empirical relationship (Khan, 2006)

(4)
K s = K s 0 / ( 1 + K x / s [ MX ] ) where KS0 = KS at [MX] = 0 (Khan and Ismail, 2010). The magnitude of the empirical constant, KX/S, is the measure of the ability of counterion, X, to expel another counterion, S, from the cationic micellar pseudophase to the aqueous phase through the occurrence of ion exchange process X/S at the cationic micellar surface. It has been shown in the earlier reports (Khan, 2006; Yusof and Khan, 2010; Khan, 2010) that Eq. (4) and a brief reaction mechanism for CTABr micellar-catalyzed reaction of Pip with PSa in terms of pseudophase micellar (PM) model can lead to Eq. (2) with respective θ and KX/S expressed by Eqs. (5) and (6), (Yusof and Khan, 2010; Khan and Sinasamy, 2011) respectively,
(5)
θ = F X / S k W MX Pip T
where kWMX[Pip]T = kobs obtained at a typical value of [MX], [Pip]T = 0.1 M and [CTABr]T = 0 as well as FX/S is an empirical constant whose value, by definition, should vary in the range >0–⩽1.0.
(6)
K X / S = K X / S / 1 + K S 0 CTABr T

In view of Eq. (2), the values of θ should be independent of [CTABr]T. Relatively more reliable calculated values of θ (Table 1) are almost independent of [CTABr]T for MX = 2-, 3- and 4-IBzNa. Mean values of FX/S, calculated from Eq. (5) with kWMX[Pip]T = 32.7 × 10−3 s−1 at 0.1 M Pip, for X = 2-, 3- and 4-IBz, (Yusof and Khan, 2010) are shown in Table 2.

Table 2 Mean values of FX/S and K X Br or R X Br for different MX in the presence of CTABr micelles.a
X [MX]oop 102 FX/S K X Br or R X Br [MX]scb mM Micelles’ structure
2-IC6H4CO2 (2-IBz) Nonzero zero 74 ± 5c 104 ± 43 11.2 ± 0.9c 8.6 ± 1.4 SRd
3-IC6H4CO2 (3-IBz) Nonzero zero 98 ± 0 115 ± 10 147 ± 13 73.2 ± 12 20e WMf
4-IC6H4CO2 (4-IBz) Nonzero zero 86 ± 4 104 ± 4 143 ± 13 86 ± 20 20e, 30g WM
3-FC6H4CO2 Nonzero 71 12.8h 70, 70h WM
4-FC6H4CO2 Nonzero 80 13.4h 70, 80h WM
2-BrC6H4CO2 Nonzero 63 8.8i SR
3-BrC6H4CO2 Nonzero 92 71i 30e WM
4-BrC6H4CO2 Nonzero 98 62i 30 WM
C6H5CO2 Zero 70 5.8j SMk,l
Cationic CTABr micelles.
The specific concentration of MX for the occurrence of the viscosity maximum of the plot of ηγ vs. [MX].
Error limits are standard deviations.
SR = short rodlike micelles.
At 15 mM CTABr.
WM = wormlike micelles.
At 5 mM CTABr (the value of [MX]sc corresponds to second maximum of the plot).
SM = spherical micelles.

The values of KX/S at different [CTABr]T were calculated from Eq. (6) with the reported value of KS0 (= 7 × 103 M−1) (Khan, 2006). These calculated values of KX/S, at different [CTABr]T for X = 2-, 3- and 4-IBz, are shown in Table 1. Relatively more reliable values of KX/S are almost independent of [CTABr]T within its range 0.005–⩽0.015 M (Table 1) and this is a requirement for the validity of Eq. (4). It has been concluded in the recent reports (Khan and Ismail, 2007; Khan, 2010) that the normalized KX/Sn (= FX/S KX/S) and KY/Sn (= FY/S KY/S) values are empirically related to the ratio KX/KY, through the relationship: RXY = KX/KY = KX/Sn/KY/Sn with KX = [XM]/([XW][Dn]) and KY = [YM]/([YW][Dn]). The values of KX/Sn (Table 1) and the reported value of 25 M−1 (Yusof and Khan, 2010) for KBr/Sn (with Br = Y) give the values of K X Br or R X Br for X = 2-, 3- and 4-IBz. These results are also shown in Table 1. The mean values of K X Br or R X Br , obtained within [CTABr]T range 0.005–⩽0.015 M for X = 2, 3- and 4-IBz, are summarized in Table 2.

Perhaps it is noteworthy that the value of KBr/Sn (= 25 M−1) has been derived from kinetic parameters obtained in the presence of spherical CTABr micelles (Khan et al., 2000). But the values of KX/Sn may be obtained, depending upon the structural features of X, in the presence of either spherical or nonspherical micelles. Thus, the value of R X Br becomes usual/conventional ion exchange constant ( K X Br ) if the value of KX/Sn is obtained in the presence of spherical micelles.

The cationic micellar structural transition from spherical to rodlike micelles (RM) and RMs+ vesicles is shown to accompany by significant increase in the degree of counterion (X = Br) binding (βX) (Ono et al., 2005; Rodriguez et al., 2009). However, although βX values for CTACl/4-XBzNa (with X = F, Cl, Br, I) systems vary only slightly with the change of X from F to I, cryo-TEM images for 0.005 M CTACl/0.003 M MX reveal the presence of only spherical micelles for X = 4-FBz while mixed spherical + long RM of different natures for X = 4-ClBz, 4-BrBz and 4-IBz (Ge et al., 2008). The values of R X Br for X = 3-ClBz (Khan and Ismail, 2009), 4-BrBz (Yusof and Khan, 2011) and 4-IBz (Table 2) are many folds larger than that for X = 4-FBz (Yusof and Khan, 2010). Similarly, the values of R X Br for X = 3-BrBz and 3-IBz are larger by respectively 1.4- and 2.8-fold than that for X = 3-ClBz (Khan and Ismail, 2009). The increase in electronegativity and polarizability of the substituent of counterions X is expected to decrease and increase the values of K X Br or R X Br , respectively. The increase in the steric requirements of X is also expected to possibly decrease the values of K X Br or R X Br . Thus, ∼10-fold larger value of R X Br for X = 4-IBz than that for X = 4-FBz may be ascribed to the combined effects of electronegativity, polarizability and steric requirements of F and I.

4.2

4.2 Rheological behavior of aqueous solutions of CTABr containing 2-, 3- and 4-IBzNa

Generally, shear viscosity (η) vs. shear rate ( γ ̇ ) plot of wormlike micellar solutions reveals four distinct regions, i.e. Newtonian, shear thinning, shear thickening and shear thinning (Ge et al., 2008). The initial Newtonian regions of Fig. 2 and Figs. S3–S5 (SD) appear to be missing presumably because these Newtonian regions are expected to appear at very low shear rates (<0.4 s−1). The rheometer used in this study could not measure the shear viscosity at γ ̇ < ∼1.0 s−1 for MX = 2-IBzNa and γ ̇ < ∼0.4 s−1 for MX = 3- and 4-IBzNa at 0.015 M CTABr. Although the plots of Fig. 2 and Figs. S3–S5 do not show the distinct presence of shear thickening regions, most of these plots do indicate regions of very low gradients (within γ ̇ range ∼25–200 s−1, Fig. S3, and ∼6–30 s−1, Fig. 2 and Figs. S4 and S5), between two different shear thinning regions at some values of [MX]. The regions of very low gradients are more apparent with MX = 2-IBzNa (Fig. S3) than those with MX = 3- and 4-IBzNa (Fig. 2 and Figs. S4 and S5). It is also evident from the plots of Fig. 2 and Figs. S3 and S5 that the plots representing initial shear thinning regions have significantly larger absolute values of gradients for MX = 2-IBzNa than those for MX = 3- and 4-IBzNa. This may be attributed to the presence of short RM for MX = 2-IBzNa and long flexible RM/WM for MX = 3- and 4-IBzNa. The flow curve at 0.01 M 2-IBzNa exhibits shear thickening while shear thickening does not exist under essentially similar conditions for MX = 3- and 4-IBzNa. Shear thickening, similar to one at 0.01 M 2-IBzNa in Fig. S3, is also exhibited by the flow curve at [MX] = 0 in Fig. S4. It is known from the literature that the aqueous solution containing <∼0.2 M (Rao et al., 1987) and <∼0.1 M CTABr Geng et al., 2005) contains only spherical micelles. Perhaps it is relevant to note that the flow curve at 0.01 M 2-IBzNa (Fig. S3) is very similar to what one would see if Taylor vortices (an unstable flow that occurs in Couette flow of low viscosity fluids at high shear rates) were present. These observations reveal the presence of spherical micelles at 0.01 M 2-IBzNa and RM (rodlike micelles) at 0.01 M MX with MX = 3- and 4-IBzNa. Nearly 13-fold smaller value of R X Br for X = 2-IBz than those for X = 3- and 4-IBz is the most probable cause for the presence of short RM for MX = 2-IBzNa and long flexible RM for MX = 3- and 4-IBzNa.

It seems noteworthy that the shapes of the flow curves (i.e., the plots of η vs. γ ̇ ) at different [MX] for MX = 2-, 3- and 4-IBzNa are significantly different from the corresponding plots for MX = 2-, 3- and 4-BrBzNa (Yusof and Khan, 2011) as well as 3- and 4-FBzNa (Yusof and Khan, 2010). The flow curves at 0.01 M MX show the presence and absence of RM for respectively MX = 3-IBzNa (Fig. 2) and 3-BrBzNa (Yusof and Khan, 2011). This distinct difference is attributed to 2-fold larger value of R X Br for X = 3-IBz than that for X = 3-BrBz (Yusof and Khan, 2011). The characteristic differences between the flow curves for MX = FBzNa (Yusof and Khan, 2010), BrBzNa (Yusof and Khan, 2011) and IBzNa may be attributed to significantly large differences in the magnitudes of R X Br for X = FBz, BrBz and IBz (Table 2).

The presence of two maxima in the plot of η 2.5 γ ̇ vs. [4-IBzNa] at 0.005 M CTABr (Fig. 3) is comparable with a recent study on rheological behavior of 0.005 M CTACl solutions mixed with [4-IBzNa] in the range 0.003–0.02 M (Ge et al., 2008). However, the plot of η 2.5 γ ̇ vs. [4-IBzNa] at 0.015 M CTABr exhibits the presence of only one maximum (Fig. 3).

Cryo-TEM image for CTACl/4-IBzNa system at 0.005 M CTACl and 0.02 M 4-IBzNa has long flexible and entangled rodlike micelles (RM) (Ge et al., 2008). Thus, it may not be unreasonable to propose that CTABr/3-IBzNa and CTABr/4-IBzNa systems have long linear and entangled RM at both 0.005 and 0.015 M CTABr. For the CTACl/4-FBzNa system at 0.005 M CTACl and 0.02 M 4-FBzNa, the cryo-TEM image has spherical and some short stiff RM (Ge et al., 2008). The value of R X Br for X = 4-FBz (Yusof and Khan, 2010) is only slightly larger than that for X = 2-IBz (Table 2). The near similarity of R X Br values for X = 2-IBz and 4-FBz, nearly 13-fold larger value of R X Br for X = 4-IBz than that for X = 2-IBz and characteristically different natures of the plots of Figs. S3 and S5 may be attributed to the probable presence of short stiff RM in CTABr/2-IBzNa system at 0.015 M CTABr and different concentrations of 2-IBzNa. It is evident from the plots of Fig. 3 that the aqueous solutions of CTABr/MX contain large number of long linear RM even at 0.003 M CTAX (X = 4-IBz).

4.3

4.3 Relationship between the magnitudes of R X Br and X-induced micellar growth

Since 1976, the attempts of finding new viscoelastic additives have relied upon the qualitative perception that unusually strong counterionic (X) binding to ionic micelles is the main cause for the X-induced viscoelastic wormlike micellar behavior of aqueous ionic surfactant solutions containing counterionic salts (MX) (Lu et al., 1998; Bijma and Engberts, 1997; Ali et al., 2009; Vermathen et al., 2002; Davies et al., 2006; Gravsholt, 1976; Oelschlaeger et al., 2010; Abezgauz et al., 2010; Takeda et al., 2011; Penfold et al., 2004). Relatively more reliable values of R X Br for X = 2-, 3- and 4-IBz (Table 2) indicate, perhaps for the first time for these counterions (X), a quantitative correlation between the values of R X Br and X–induced formation of short RM for X = 2-IBz as well as long linear and entangled RM for X = 3- and 4-IBz at the constant [CTABr] (= 0.005 or 0.015 M) and varying values of [MX]. The value of [MX]sc represents the specific value of [MX] at which maximum density of entangled RM occurs at a constant [CTABr] (= 0.015 M) in the plot of η γ ̇ vs. [MX]. It may be noteworthy that the values of [MX]sc remain unchanged with the change of γ ̇ from ∼2 to 1000 s−1. Thus, if the density of entangled RM formation increases with the increase of the ionic micellar binding constants of counterions (X) at a constant [CTABr] then the values of [MX]sc should decrease with the increase of R X Br . The listed values of [MX]sc vs. R X Br of Table 2 for X = 3-, 4-FBz, 3-, 4-BrBz and 3-, 4-IBz support this conclusion.

5

5 Conclusions

(i) The new and perhaps interesting findings of the present study are the experimentally determined values of R X Br of 11, 147 and 143 for X = 2-, 3- and 4-IBz, respectively. (ii) One typical advantage of the SEK method is that it gives the values of both K X Br and R X Br while all the other existing methods, to the best of our knowledge, can give only the values of K X Br and not R X Br . (iii) Rheometric data of this study show the presence of short rigid rodlike micelles for X = 2-IBz and long linear and entangled rodlike micelles for X = 3- and 4-IBz. (iv) Here in this article, a quantitative correlation is presented between the values of R X Br and X-induced micellar structures of short rigid rodlike micelles for X = 2-IBz and long linear and entangled RM micelles for X = 3- and 4-IBz at [MX] range ∼0.005 or 0.01–0.02 M in the presence of 0.005 or 0.015 M CTABr. (v) The positions of maxima in the plots of η γ ̇ vs. [MX] remain essentially unchanged with the change of γ ̇ within its range 2 to 103 s−1. (vi) The kinetic validity of Eq. (3) constitutes an indirect evidence for the occurrence of two or more than two independent ion exchange processes under the present reaction conditions.

Acknowledgements

The authors thank the University of Malaya (UM) for financial assistance through research grant HIR UM/MOHE/SC/07, RG022/09AFR, and the Centre of Ionic Liquids, UM for the permission to carry out the rheological study.

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Appendix A

Supplementary data

Supplementary data associated with this article can be found, in the online version, at http://dx.doi.org/10.1016/j.arabjc.2013.10.020.

Appendix A

Supplementary data

Supplementary data 1

Supplementary data 1

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