art%3A10.1007%2Fs10953-015-0305-5

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Experimental Study and Modeling of the Refractive Indices in Binary and Ternary Mixtures of Water with Methanol, Ethanol and Propan-1-ol at 293.15 K Marlon Martı ´nez-Reina Eliseo Amado-Gonza ´lez Wilfred Gome ´z-Jaramillo Received: 9 August 2014 / Accepted: 1 November 2014 / Published online: 24 February 2015 Ó Springer Science+Business Media New York 2015 Abstract Refractive indices of ternary mixtures of water ? methanol ? (ethanol or propan-1-ol), (water or methanol) ? ethanol ? propan-1-ol and their binary mixtures have been measured at 293.15 K and at atmospheric pressure over the whole composition range. The refractive index deviations were calculated and fitted to the Redlich–Kister equation for binary mixtures, and the Cibulka equation for ternary mixtures. Furthermore, we demonstrate that the refractive index of the associated ternary mixtures can be estimated with relative errors from 0.036 to 0.861 % by using the several mixing rules and the refractive indices of the corresponding pure components. The behavior of refractive indices is associated with solvent–solvent interactions and the formation of clusters. Keywords Refractive index Ternary mixtures Refractive index deviations Mixing rules Clusters 1 Introduction The refractive indices of pure components and their mixtures are an optical property of matter that allows control of processes in the chemical, petrochemical and pharmaceutical industries, and its importance is well known. For some specific scientific applications, the required accuracy is very high and requires precise measurements [1]. Since the refractive index of a liquid at the sodium D line light, n D , is a property easy to measure with good accuracy, it has been connected with other thermo physical properties, such as surface tension and density, by empirical and theoretical equations [2, 3]. A structure–property model has been found to have great potential for predicting the physicochemical properties of substances [4]. It is known that refractive index mixing rules allow estimation of the M. Martı ´nez-Reina E. Amado-Gonza ´lez (&) W. Gome ´z-Jaramillo Ibear L-307 Biofuels Laboratory, Department of Chemistry, University of Pamplona, Ciudad Universitaria, Pamplona, Colombia e-mail: [email protected] 123 J Solution Chem (2015) 44:206–222 DOI 10.1007/s10953-015-0305-5

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Transcript of art%3A10.1007%2Fs10953-015-0305-5

  • Experimental Study and Modeling of the RefractiveIndices in Binary and Ternary Mixtures of Waterwith Methanol, Ethanol and Propan-1-ol at 293.15 K

    Marlon Martnez-Reina Eliseo Amado-Gonzalez Wilfred Gomez-Jaramillo

    Received: 9 August 2014 / Accepted: 1 November 2014 / Published online: 24 February 2015 Springer Science+Business Media New York 2015

    Abstract Refractive indices of ternary mixtures of water ? methanol ? (ethanol orpropan-1-ol), (water or methanol) ? ethanol ? propan-1-ol and their binary mixtures have

    been measured at 293.15 K and at atmospheric pressure over the whole composition range.

    The refractive index deviations were calculated and fitted to the RedlichKister equation

    for binary mixtures, and the Cibulka equation for ternary mixtures. Furthermore, we

    demonstrate that the refractive index of the associated ternary mixtures can be estimated

    with relative errors from 0.036 to 0.861 % by using the several mixing rules and the

    refractive indices of the corresponding pure components. The behavior of refractive indices

    is associated with solventsolvent interactions and the formation of clusters.

    Keywords Refractive index Ternary mixtures Refractive index deviations Mixingrules Clusters

    1 Introduction

    The refractive indices of pure components and their mixtures are an optical property of

    matter that allows control of processes in the chemical, petrochemical and pharmaceutical

    industries, and its importance is well known. For some specific scientific applications, the

    required accuracy is very high and requires precise measurements [1]. Since the refractive

    index of a liquid at the sodium D line light, nD, is a property easy to measure with good

    accuracy, it has been connected with other thermo physical properties, such as surface

    tension and density, by empirical and theoretical equations [2, 3]. A structureproperty

    model has been found to have great potential for predicting the physicochemical properties

    of substances [4]. It is known that refractive index mixing rules allow estimation of the

    M. Martnez-Reina E. Amado-Gonzalez (&) W. Gomez-JaramilloIbear L-307 Biofuels Laboratory, Department of Chemistry, University of Pamplona, CiudadUniversitaria, Pamplona, Colombiae-mail: [email protected]

    123

    J Solution Chem (2015) 44:206222DOI 10.1007/s10953-015-0305-5

  • refractive index of a mixture from the refractive indices of the pure components. Hellers

    work [5] shows that these mixing rules can be used to predict the density or excess volumes

    of a mixture from its refractive index or vice versa.

    In recent years some workers have studied the refractive indices of (binary or ternary)

    liquid mixtures and analyzed the applicability of the refractive index mixing rules: 19

    binary mixtures of various polarities [6], 73 binary mixtures containing various groups of

    organic compounds [7, 8], (water ? ethanol ? k-ethylene glycol) (when k is mono, di or

    tri) [1], isomers of butanol with n-hexane, and 1-chlorobutane [9], isomers of chlorobu-

    tanes and butanols [10], diethyl malonate ? (dimethylformamide, hexane, tetrahydrofuran

    or 1,4-dioxane) [11], tetrahydrofuran ? (methanol or o-cresol) [12], eucalyptol ? hydro-

    carbons [13], ethanol ? n-alkane mixtures [14], chlorobenzene ? n-hexane ? (n-heptane

    or n-octane) [15], cyclohexane ? toluene ? methanol [16], and tetralin ? isobutylben-

    zene ? dodecane [17]. Alcohols are polar molecules, self-associated by hydrogen bonding

    of their hydroxyl groups [18]. The hydrogen bonding gives the alcohols the possibility of

    interacting with other substances to change their structure. The applications of alcohols in

    the food industry, and pharmaceutical uses as co-surfactants in micro emulsions, are still

    under development [19].

    Among the thermo physical properties, refractive indices of water with alcohols in

    binary and ternary systems are expected to show complex behavior, due to the inter-

    molecular interactions [20]. Therefore, the binary systems of water with methanol, ethanol

    or propan-1-ol, and their ternary systems are of great interest.

    In the present paper, refractive indices at 293.15 K are reported for six binary mixtures:

    water ? (methanol, ethanol or propan-1-ol), methanol ? (ethanol or propan-1-ol), etha-

    nol ? propan-1-ol, and for four ternary mixtures: water ? methanol ? (ethanol or pro-

    pan-1-ol), water ? ethanol ? propan-1-ol and methanol ? ethanol ? propan-1-ol. These

    data were used to calculate the refractive index deviations, DnD, which were correlatedusing a 5-parameter RedlichKister equation [21] for binary mixtures and the Cibulka

    equation [22] for ternary mixtures. Finally, we have used several mixing rules, those of

    LorentzLorenz [23, 24], GladstoneDale [25], Eykman [26], Newton [27] and Oster [28],

    to predict refractive indices. The accuracy of the mixing rules for determination of re-

    fractive indices is analyzed and cluster formation is predicted for the ternary mixtures.

    2 Experimental

    Densities of the pure liquids were measured by using a pycnometer having bulb volume of

    approximately 10 cm3 and capillary with internal diameter of 1 mm. First, the pycnometer

    was calibrated with distilled water of known density, and then it was filled with pure liquid

    and immersed in a thermostatic bath. The bath temperature was monitored to 0.01 K with

    a calibrated thermometer. In addition, all of the measurements were conducted in a room

    with controlled air temperature. About 120 min later, the sample was weighed. A cover

    was used in order to prevent the samples from absorbing water or evaporating. The

    uncertainly of the density measurements was estimated to be 0.05 %. Mixtures were

    prepared by mixing the appropriate volumes of liquids in specially designed ground glass

    air-tight ampules and weighed in single pan balance (Ohaus electronic balance) to an

    accuracy of 0.0001 g. Preferential evaporation losses of solvent from the mixture were

    kept to a minimum as evidenced by repeated measurements of thermo physical properties

    over an interval of 23 days, during which time no change in physical properties were

    observed. The composition of the mixtures were calculated in mole fraction with atomic

    J Solution Chem (2015) 44:206222 207

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  • weights recommended by IUPAC in 2000 [29]. The possible error in mole fraction is

    estimated to be around 0.0001. Refractive indices for the sodium D line were measured

    using Abbes refractometer (CARL ZEISS, Model A, Germany). Water was circulated into

    the instrument from the thermostatically controlled bath. The current temperature of the

    measurement prism of the refractometer was monitored using a built-in instrument with an

    uncertainty 0.1 K. The refractometer was calibrated by measuring the refractive indices

    of triply distilled water and ethanol at 293.15 K. The accuracy in the refractive index

    measurements is 0.0001 U. The sample mixtures were directly injected into the prism

    assembly of the instrument by means of an air-tight hypodermic syringe. An average of

    three to five measurements was taken for a sample mixture. The source of our chemicals

    and our measured values at 293.15 K of two physical properties of the pure compounds,

    densities and refractive indices, are compared with literature [3034] values in Table 1.

    The refractive indices of the binary systems water(1) ? propan-1-ol(2), water(1) ?

    ethanol(2) and water(1) ? methanol(2) are compared with literature data in Fig. 1.

    3 Results and Discussion

    The experimental results of mole fraction, xi, refractive indices, nD, refractive index de-

    viations, DnD, at 293.15 K for all binary mixtures are reported in Table 2. The refractiveindex deviations were evaluated for each composition point, using the following equation:

    DnD nD Xn

    i1xinD;i 1

    where nD is the refractive index of the mixture and the corresponding quantity with

    subscript i refers to the corresponding pure chemicals. The experimental DnD values werecorrelated using a 5-parameter RedlichKister equation:

    DnD x1x2Xm

    p0Apx1 x2p 2

    where x is the molar fraction, A0, A1, A2, A3 and A4 are the RedlichKister parameters

    obtained by least-squares method, and m = 4 is the degree of the polynomial expansion.

    The parameters calculated using Eq. 2 are listed in Table 3. On Fig. 2, the refractive index

    deviations are shown for the binary mixtures. The physical property values of these so-

    lutions can be affected by two factors. The first factor is the concentration units (molar,

    molalor mole fraction) of the solute in the mixture. The second factor is the strength of

    Table 1 Experimental and literature values [3034] of densities, q, and refractive indices, nD, of the purecompounds at 293.15 K

    Compound nD(experimental)

    nD(literature)

    q (experimental)gcm-3

    q (literature)gcm-3

    Water, deionized reagent grade 3 1.3330 1.3330 [30] 0.9981 0.9982 [33]

    Methanol (Sigma-Aldrich, 99.9 %) 1.3299 1.32941 [31] 0.7912 0.79115 [31]

    Ethanol (Carlo Erba, 99.8 %) 1.3618 1.3620 [30] 0.7895 0.78970 [34]

    Propan-1-ol (Merck, 99.5 %) 1.3853 1.38512 [32] 0.8036 0.80360 [34]

    208 J Solution Chem (2015) 44:206222

    123

  • bonds between solvent and solute molecules due to the values of polarity (dipoledipole

    interaction and the H-bonds) and the electrical charge of solute molecules [35].

    It can be observed from the experimental data in Table 2 and Fig. 2 that, over the whole

    composition range for all aqueous solutions of this study at T = 293.15 K, the variation

    of DnD is positive and follows this order: DnDCH3OH\DnDCH3CH2OH\DnDCH3CH2CH2OH for these solutions the values of DnD increase with the size of the(R) group. On Fig. 2, a maximum is observed at xM = xmethanol = 0.3961 for the mixture

    water ? methanol. Takamuku et al. [37] found, from analysis of radial distribution

    functions (RDF) for methanol ? water mixtures, three peaks at xM = 0.4 and 298.15 K

    that were analyzed were the result of the intermolecular interactions of methanol chain

    clusters and the second-neighbor interactions in the tetrahedral-like structure of water [38].

    Positive deviations of the excess values of binary mixtures should be the result of dis-

    persion forces and non-specific physical (weak) interactions [39]. Nagasaka et al. [40]

    found that the total energy of the binary solution is stabilized by the network structure of

    water with the methanol clusters. But, the effect of water molecules on the methyl group of

    methanol may depend on whether water molecules are free or associated in the network.

    For the mixture ethanol ? water, it is found on Fig. 2 that a maximum occurs at xE =

    xEthanol = 0.2972. Matsumoto et al. found that both ethanol chain clusters and water

    clusters are formed in ethanolwater mixture at xE = 0.3 and 298.15 from RDF analysis

    [41]. For the mixture water ? propan-1-ol, the maximum is found at xp,1 = xpropan-1-

    Fig. 1 Comparison between the experimental data and values from literature. Water(1) ? methanol(2):(filled circle) this work at 293.15 K, (circle) Ref. [35] at 292.15 K. Water(1) ? ethanol(2): (filled square)this work at 293.15 K, (square) Ref. [35] at 292.15 K, (cross) Ref. [36] at 293.15 K. Water(1) ? propan-1-ol(2): (filled diamond) this work at 293.15 K, (diamond) Ref. [35]

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  • Table 2 Experimental refractiveindices and their deviations fromideality at 293.15 K for the in-vestigated binary mixtures

    x1 nD DnD x1 nD DnD

    Water(1) ? methanol(2)

    0.0000 1.3299 0.0000 0.6039 1.3436 0.0118

    0.1007 1.3326 0.0023 0.6901 1.3432 0.0111

    0.2044 1.3359 0.0054 0.7941 1.3412 0.0088

    0.2910 1.3385 0.0076 0.8952 1.3376 0.0049

    0.4034 1.3411 0.0099 1.0000 1.3330 0.0000

    0.5003 1.3423 0.0108

    Water(1) ? ethanol(2)

    0.0000 1.3618 0.0000 0.5983 1.3645 0.0199

    0.1037 1.3640 0.0052 0.7028 1.3626 0.0210

    0.2064 1.3649 0.0090 0.7932 1.3584 0.0194

    0.3047 1.3657 0.0127 0.8979 1.3488 0.0128

    0.3939 1.3660 0.0156 1.0000 1.3330 0.0000

    0.4937 1.3656 0.0180

    Water(1) ? propan-1-ol(2)

    0.0000 1.3853 0.0000 0.5979 1.3762 0.0221

    0.1080 1.3843 0.0046 0.7225 1.3708 0.0233

    0.2181 1.3834 0.0095 0.7939 1.3662 0.0224

    0.2737 1.3828 0.0118 0.8999 1.3552 0.0169

    0.4030 1.3809 0.0167 1.0000 1.3330 0.0000

    0.4998 1.3789 0.0197

    Methanol(1) ? ethanol(2)

    0.0000 1.3618 0.0000 0.6108 1.3447 0.0024

    0.1099 1.3591 0.0008 0.7062 1.3413 0.0020

    0.1727 1.3576 0.0013 0.8078 1.3373 0.0012

    0.3292 1.3535 0.0022 0.9010 1.3338 0.0007

    0.4003 1.3514 0.0024 1.0000 1.3299 0.0000

    0.5065 1.3481 0.0024

    Methanol(1) ? propan-1-ol(2)

    0.0000 1.3853 0.0000 0.6007 1.3596 0.0076

    0.1177 1.3809 0.0021 0.7023 1.3534 0.0070

    0.1798 1.3788 0.0035 0.7721 1.3485 0.0059

    0.3147 1.3738 0.0059 0.8971 1.3387 0.0031

    0.3760 1.3710 0.0065 1.0000 1.3299 0.0000

    0.4801 1.3660 0.0073

    Ethanol(1) ? propan-1-ol(2)

    0.0000 1.3853 0.0000 0.6134 1.3720 0.0011

    0.1077 1.3825 -0.0003 0.6879 1.3701 0.0010

    0.2227 1.3803 0.0002 0.7961 1.3672 0.0006

    0.2797 1.3792 0.0005 0.8930 1.3646 0.0003

    0.3880 1.3771 0.0009 1.0000 1.3618 0.0000

    0.5007 1.3747 0.0012

    210 J Solution Chem (2015) 44:206222

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  • ol = 0.2775 as seen in Fig. 2. It is found that the mixtures from C1 to C3 show that the

    maximum moves to a more water-rich zone (xw = xwater = 0.6039 for methanol to

    xw = 0.7225 for propan-1-ol). Thus cluster formation may be expected at these

    concentrations.

    In this work, the binary mixtures with alcohols show values of DnD lower than thosereported for aqueous mixtures. The variation of DnD in these mixtures is:DnDCH3CH2OH + CH3CH2CH2OH\DnDCH3OH + CH3CH2OH\DnDCH3OH +CH3CH2CH2OH; the mixture that deviates least from ideality is ethanol(1) ? propan-1-ol(2). Our results for this mixture, as a function of concentration at 298.15 K, coincide well

    with those reported in the literature [32].

    The experimental results of mole fraction, xi, refractive indices, nD, refractive index

    deviations, DnD, at 293.15 K for all ternary mixtures are reported in Table 4. The re-fractive index deviations for the ternary mixtures have been fitted by the Cibulka equation:

    DnD DnD;bin x1x21 x1 x2B1 B2x1 B3x2 3

    DnD;bin x1x2Xm

    p0Apx1 x2p x1x3

    Xm

    q0Aqx1 x3q x2x3

    Xm

    r0Arx2 x3r 4

    where the Ai are binary solution parameters of a RedlichKister type equation for the

    constituent binary mixtures, Bi are parameters of the Cibulka equation and xi is molar

    fraction of component i at the ternary data composition. The parameters calculated using

    Eq. 3 are listed in Table 5. The root-mean-square deviations (r) were computed usingEq. 5, where ncalc is the calculated value of refractive index, nexp is the measured value of

    the refractive index, and NDAT is the number of experimental data values:

    r PNDAT

    i1 nexp ncalc2NDAT

    !1=25

    Figures 3, 4, 5, and 6 show that the refractive index deviations for all the ternary

    mixtures are positive over the whole composition range. The results are consistent with

    Table 3 RedlichKister parameters Ai (Eq. 2) and the standard deviations (r, Eq. 5)

    A0 A1 A2 A3 A4 r

    Water(1) ? methanol(2)

    0.04414 0.01977 0.00840 -0.00547 -0.02717 0.00010

    Water(1) ? ethanol(2)

    0.07266 0.04826 0.04477 0.01016 -0.00877 0.00016

    Water(1) ? propan-1-ol(2)

    0.07904 0.05310 0.03719 0.05223 0.03536 0.00009

    Methanol(1) ? ethanol(2)

    0.00998 -0.00036 -0.00199 -0.00053 -0.00259 0.00006

    Methanol(1) ? propan-1-ol(2)

    0.02971 0.00779 0.00436 0.00122 -0.01539 0.00005

    Ethanol(1) ? propan-1-ol(2)

    0.00467 0.00151 -0.00615 0.00373 -0.00237 0.00002

    J Solution Chem (2015) 44:206222 211

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  • those reported in binary mixtures; aqueous solutions show a greater deviation than the

    mixtures composed of the three alcohols: methanol(1) ? ethanol(2) ? propan-1-ol(3). The

    maximum refractive index deviation (DnD) for the ternary mixtures in Table 6 variesin the order: methanol ? ethanol ? propan-1-ol \ water ? methanol ? ethanol \ water ?methanol ? propan-1-ol = water ? ethanol ?propan-1-ol. The refractive index de-

    viations of the aqueous mixtures are due to hydrogen bond interactions between the water

    or methanol molecule, ethanol and propanol molecules.

    Reiss et al. [42] considered that the increase of the refractive indices for the mixtures of

    solvents is explained as the result of both energetic and structural effects where the en-

    hancement of London disperse forces plays an important role. We may expect that these

    maxima in the water-rich zone should reflect cluster structures. In the mixtures of solvents

    with water, Fontao et al. considered that positive values of the refractive index deviation on

    mixing may be due to two opposing factors: (a) the hydrogen-bond interaction between

    solute and solvent for each mixture, and (b) the steric hindrance of aliphatic residues [32].

    The positive refractive index deviation decrease in the following order for the binary

    mixtures: water(1) ? propan-1-ol(2) [ water(1) ? ethanol(2)[ water(1) ? methanol(2) [methanol(1) ? propan-1-ol(2) [ methanol(1) ? ethanol(2) [ ethanol(1) ? propan-1-ol(2).This suggests that the steric hindrance of aliphatic residues affects the increase for alcohol

    mixtures where hydrogen bonding is not strong. The isolines of DnD obtained from Cibulkaequation, for the four ternary systems, are plotted at the bottom of Figs. 3, 4, 5, and 6.

    The following equations were used for quantitative determination of refractive indices

    of ternary mixtures:

    Fig. 2 Curves of refractive index deviations at 293.15 K for the systems: (filled circle) wa-ter(1) ? methanol(2), (filled square) water(1) ? ethanol(2), (filled diamond) water(1) ? propan-1-ol(2),(circle) methanol(1) ? ethanol(2), (square) methanol(1) ? propan-1-ol(2), and (diamond) ethanol(1) ?propan-1-ol(2). The experimental data were fitted with RedlichKister type polynomials (solid line)

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  • Table 4 Experimental refractive indices and their deviations from ideality at 293.15 K for the ternarymixtures

    x1 x2 nD DnD x1 x2 nD DnD

    Water(1) ? methanol(2) ? ethanol(3)

    0.1047 0.7951 1.3363 0.0029 0.2865 0.3089 1.3548 0.0111

    0.1076 0.6916 1.3407 0.0041 0.2865 0.2154 1.3581 0.0114

    0.0956 0.6055 1.3442 0.0045 0.2854 0.1088 1.3613 0.0112

    0.1107 0.5061 1.3479 0.0054 0.3941 0.4995 1.3453 0.0108

    0.0997 0.4133 1.3512 0.0055 0.4357 0.3762 1.3504 0.0132

    0.0906 0.3139 1.3542 0.0050 0.3976 0.3060 1.3540 0.0134

    0.1112 0.2032 1.3576 0.0055 0.3745 0.2117 1.3580 0.0137

    0.1060 0.0784 1.3608 0.0046 0.4103 0.1096 1.3613 0.0148

    0.1873 0.7079 1.3399 0.0061 0.5118 0.3821 1.3479 0.0130

    0.1896 0.6047 1.3444 0.0074 0.5146 0.2914 1.3526 0.0149

    0.1659 0.5231 1.3478 0.0075 0.4912 0.1991 1.3573 0.0160

    0.1847 0.4154 1.3517 0.0085 0.4746 0.1345 1.3601 0.0163

    0.2151 0.3006 1.3558 0.0098 0.5879 0.2982 1.3497 0.0143

    0.2217 0.2004 1.3590 0.0100 0.5995 0.2075 1.3543 0.0164

    0.2302 0.1013 1.3618 0.0099 0.6175 0.0963 1.3594 0.0185

    0.3283 0.5718 1.3431 0.0090 0.7211 0.1842 1.3498 0.0146

    0.3045 0.4992 1.3470 0.0099 0.7007 0.1020 1.3541 0.0157

    0.3069 0.3988 1.3513 0.0111 0.7960 0.0961 1.3506 0.0148

    Water(1) ? methanol(2) ? propan-1-ol(3)

    0.0863 0.8045 1.3417 0.0055 0.3021 0.2980 1.3689 0.0159

    0.0963 0.6945 1.3502 0.0084 0.3168 0.1699 1.3750 0.0157

    0.1015 0.5736 1.3584 0.0102 0.2943 0.0959 1.3784 0.0138

    0.0919 0.5028 1.3628 0.0102 0.4025 0.4686 1.3529 0.0146

    0.0988 0.4011 1.3681 0.0102 0.3713 0.4096 1.3586 0.0154

    0.0911 0.2987 1.3731 0.0091 0.3712 0.3088 1.3659 0.0171

    0.0990 0.1948 1.3772 0.0079 0.3851 0.2037 1.3715 0.0176

    0.0945 0.0990 1.3807 0.0058 0.3860 0.0919 1.3769 0.0169

    0.1844 0.6978 1.3459 0.0089 0.5135 0.3737 1.3539 0.0162

    0.1789 0.6108 1.3531 0.0110 0.4737 0.3105 1.3616 0.0183

    0.1505 0.4964 1.3617 0.0118 0.4886 0.2065 1.3680 0.0197

    0.2129 0.3967 1.3658 0.0136 0.5071 0.0956 1.3738 0.0203

    0.1915 0.3185 1.3705 0.0129 0.5726 0.3211 1.3547 0.0171

    0.1524 0.2349 1.3751 0.0108 0.5769 0.2244 1.3628 0.0201

    0.1803 0.1467 1.3782 0.0105 0.5939 0.0980 1.3706 0.0218

    0.2686 0.6308 1.3474 0.0111 0.6953 0.1982 1.3564 0.0184

    0.2953 0.4885 1.3571 0.0143 0.7502 0.0774 1.3630 0.0212

    0.2787 0.4089 1.3630 0.0149 0.7724 0.1326 1.3555 0.0179

    Water(1) ? ethanol(2) ? propan-1-ol(3)

    0.0843 0.8128 1.3663 0.0045 0.3232 0.2841 1.3758 0.0141

    0.1028 0.6966 1.3692 0.0056 0.2865 0.1968 1.3783 0.0126

    0.0962 0.6005 1.3718 0.0056 0.2760 0.1176 1.3801 0.0120

    0.1086 0.4907 1.3744 0.0063 0.4219 0.4789 1.3681 0.0161

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  • Table 5 Parameters, Bi, of the Cibulka equation for the ternary mixtures together with the correspondingstandard deviations, r

    System B1 B2 B3 r

    Water(1) ? methanol(2) ? ethanol(3) -0.02015 -0.11273 -0.01606 0.00050

    Water(1) ? methanol(2) ? propan-1-ol(3) -0.02098 -0.00227 0.01776 0.00025

    Water(1) ? ethanol(2) ? propan-1-ol(3) 0.02870 -0.35314 -0.02009 0.00035

    Methanol(1) ? ethanol(2) ? propan-1-ol(3) 0.01070 0.01264 0.00850 0.00032

    Table 4 continued

    x1 x2 nD DnD x1 x2 nD DnD

    0.0920 0.4001 1.3766 0.0055 0.3748 0.4140 1.3712 0.0152

    0.1044 0.2894 1.3787 0.0057 0.3941 0.3193 1.3732 0.0160

    0.1149 0.1966 1.3806 0.0059 0.3910 0.2006 1.3762 0.0161

    0.0814 0.1001 1.3827 0.0040 0.4006 0.1017 1.3782 0.0162

    0.1890 0.6961 1.3679 0.0088 0.5059 0.3967 1.3679 0.0184

    0.1866 0.6005 1.3704 0.0090 0.4828 0.2990 1.3713 0.0183

    0.1846 0.4881 1.3733 0.0091 0.4783 0.2045 1.3739 0.0184

    0.1893 0.3977 1.3754 0.0093 0.4958 0.1028 1.3759 0.0189

    0.1892 0.2879 1.3777 0.0091 0.5740 0.3227 1.3672 0.0195

    0.1791 0.1900 1.3798 0.0083 0.6029 0.1978 1.3698 0.0207

    0.1875 0.1176 1.3812 0.0085 0.5694 0.1140 1.3735 0.0207

    0.2835 0.5994 1.3684 0.0120 0.6878 0.2121 1.3654 0.0211

    0.2642 0.4958 1.3716 0.0118 0.6975 0.1095 1.3680 0.0218

    0.2915 0.3812 1.3741 0.0130 0.8089 0.0944 1.3610 0.0202

    Methanol(1) ? ethanol(2) ? propan1-ol(3)

    0.0947 0.7928 1.3634 0.0020 0.2811 0.2982 1.3679 0.0052

    0.0822 0.7133 1.3662 0.0022 0.2681 0.2290 1.3702 0.0051

    0.1009 0.5978 1.3685 0.0028 0.3126 0.1124 1.3712 0.0059

    0.0738 0.5123 1.3720 0.0028 0.3948 0.4945 1.3556 0.0038

    0.0988 0.3997 1.3736 0.0032 0.4061 0.3906 1.3584 0.0048

    0.0900 0.3069 1.3761 0.0030 0.4027 0.2873 1.3618 0.0056

    0.0948 0.2020 1.3780 0.0027 0.4085 0.1935 1.3641 0.0060

    0.0885 0.1005 1.3803 0.0023 0.4061 0.1189 1.3664 0.0064

    0.2027 0.6831 1.3608 0.0028 0.4794 0.4202 1.3535 0.0046

    0.2020 0.5960 1.3634 0.0033 0.5060 0.3082 1.3556 0.0056

    0.1832 0.5127 1.3667 0.0036 0.5185 0.1997 1.3583 0.0064

    0.2141 0.3850 1.3688 0.0044 0.5048 0.0997 1.3622 0.0072

    0.1881 0.3063 1.3718 0.0041 0.5823 0.2947 1.3509 0.0048

    0.1891 0.2083 1.3742 0.0043 0.6050 0.1999 1.3532 0.0061

    0.1766 0.1143 1.3767 0.0039 0.5941 0.1090 1.3568 0.0070

    0.2862 0.5990 1.3590 0.0036 0.7066 0.1946 1.3459 0.0043

    0.3023 0.5087 1.3607 0.0041 0.6997 0.0981 1.3505 0.0063

    0.3015 0.4011 1.3639 0.0047 0.7724 0.1205 1.3440 0.0043

    214 J Solution Chem (2015) 44:206222

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  • LorentzLorenz (LL):

    n2 1n2 2

    Xk

    i1

    n2i 1n2i 2

    /i 6

    GladstoneDale (GD):

    n 1 Xk

    i1ni 1/i 7

    Fig. 3 Refractive index deviations and isolines at 293.15 K for the ternary systemwater(1) ? methanol(2) ? ethanol(3)

    J Solution Chem (2015) 44:206222 215

    123

  • Eykman (Eyk):

    n2 1n2 0:4

    Xk

    i1

    n2i 1n2i 0:4

    /i 8

    Fig. 4 Refractive index deviations and isolines at 293.15 K for the ternary system water(1) ?methanol(2) ? propan-1-ol(3)

    216 J Solution Chem (2015) 44:206222

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  • Newton (Nw):

    n2 1 Xk

    i1n2i 1/i 9

    Fig. 5 Refractive index deviations and isolines to 293.15 K for the ternary system water(1) ?ethanol(2) ? propan-1-ol(3)

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  • Oster (Os):

    n2 12n2 1n2

    Xk

    i1

    n2i 12n2i 1n2i

    /i 10

    Here n is the refractive index of the mixtures, ni is the refractive index of the corresponding

    pure components i, k is the number of the mixture components, and /i is the volumefraction of component i:

    Fig. 6 Refractive index deviations at isolines to 293.15 K for the ternary system methanol(1) ? etha-nol(2) ? propan-1-ol(3)

    218 J Solution Chem (2015) 44:206222

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  • /i xiViPki1 xiVi

    11

    where xi is the mole fraction of the component i, and Vi is the molar volume of the

    component i. In order to estimate the ability of the mixing rule Eqs. 610 to predict

    refractive indices, the following quantities were analyzed: average absolute deviations

    (AAD) and maximal deviation (M Dev),

    AAD 100NDAT

    XM

    i1

    npred nexpnexp

    12

    MDev 100: max npred nexpnexp

    13

    where npred is the predicted value of the refractive index and nexp is the measured value.

    The AAD and M Dev quantities can be also viewed as mean and maximal relative errors.

    The values of AADand MDev are shown in Table 7. Average absolute deviations (AAD

    values) for all mixtures do not exceed 0.50 %. From the analysis of AAD of the ex-

    perimental refractive indices using the L-L, G-D, Eyk, Nw or Os equations, the following

    sequence was found: water(1) ? methanol(2) ? ethanol(3) [ water(1) ? methanol(2) ?propan-1-ol(3) * water(1) ? ethanol(2) ? propan-1-ol(3) [ methanol(1) ? ethanol(2) ?propan1-ol(3). This behavior suggests that the hydrogen bonding interaction effect de-

    creases for alcohol mixtures. The maximal deviation M Dev in all the mixtures is lower

    than 0.9 %. The predictions obtained using these mixing rules are very similar. The values

    predicted by the Newton mixing rule display better agreement with the experimental values

    Table 6 The maximum refractive index deviations (DnD) for the ternary mixtures at 293.15 K

    System DnDmax x1 x2 x3

    Water(1) ? methanol(2) ? ethanol(3) 0.0185 0.6175 0.0963 0.2862

    Water(1) ? methanol(2) ? propan-1-ol(3) 0.0218 0.5939 0.0980 0.3081

    Water(1) ? ethanol(2) ? propan-1-ol(3) 0.0218 0.6975 0.1095 0.1930

    Methanol(1) ? ethanol(2) ? propan-1-ol(3) 0.0072 0.5048 0.0997 0.3955

    Table 7 Average absolute deviations (AAD) and maximal deviation (M Dev) of the experimental re-fractive indices from the estimated results using the LorentzLorenz (LL), GladstoneDale(GD), Eykman(Eyk), Newton (Nw) and Oster (Os) equations

    System LL GD Eyk Nw Os

    Water(1) ? methanol(2) ? ethanol(3) AAD 0.495 0.490 0.492 0.485 0.488

    M Dev 0.861 0.857 0.858 0.852 0.855

    Water(1) ? methanol(2) ? propan-1-ol(3) AAD 0.315 0.300 0.305 0.283 0.292

    M Dev 0.730 0.716 0.721 0.701 0.709

    Water(1) ? ethanol(2) ? propan-1-ol(3) AAD 0.306 0.299 0.302 0.292 0.296

    M Dev 0.686 0.676 0.680 0.665 0.670

    Methanol(1) ? ethanol(2) ? propan-1-ol(3) AAD 0.013 0.017 0.016 0.024 0.020

    M Dev 0.036 0.050 0.045 0.065 0.057

    J Solution Chem (2015) 44:206222 219

    123

  • of the refractive indices for aqueous mixtures, whereas in the ternary mixture of alcohols

    the best prediction is with LorentzLorenz mixing rule.

    4 Conclusions

    We reported measurements of refractive indices at 293.15 K for six binary mixtures

    (water ? methanol, water ? ethanol, water ? propan-1-ol, methanol ? ethanol, metha-

    nol ? propan-1-ol, ethanol ? propan-1-ol) and four ternary mixtures (water ?

    methanol ? ethanol, water ? methanol ? propan-1-ol, water ? ethanol ? propan-1-ol,

    methanol ? ethanol ? propan-1-ol); the refractive index deviations calculated from the

    experimental data of refractive indices are appropriately represented with the RedlichKister

    equation for binary mixtures and with the Cibulka equation in ternary mixtures. The de-

    viations of refractive indices are higher in aqueous ? alcohol mixtures compared with the

    alcohol ? alcohol mixtures.

    Mixing rules including the LorentzLorenz, GladstoneDale, Eykman, Newton and

    Oster formulas were used for predicting the refractive indices of ternary mixtures. We have

    demonstrated that the refractive indices provided by all the mixing rules reproduce the

    measured values with a maximal relative error of 0.861 %.

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    Experimental Study and Modeling of the Refractive Indices in Binary and Ternary Mixtures of Water with Methanol, Ethanol and Propan-1-ol at 293.15 KAbstractIntroductionExperimentalResults and DiscussionConclusionsReferences