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<article article-type="research-article" dtd-version="1.1" specific-use="sps-1.7" xml:lang="en" xmlns:mml="http://www.w3.org/1998/Math/MathML" xmlns:xlink="http://www.w3.org/1999/xlink">
	<front>
		<journal-meta>
			<journal-id journal-id-type="publisher-id">rccqf</journal-id>
			<journal-title-group>
				<journal-title>Revista Colombiana de Ciencias Químico - Farmacéuticas</journal-title>
				<abbrev-journal-title abbrev-type="publisher">Rev. colomb. cienc. quim. farm.</abbrev-journal-title>
			</journal-title-group>
			<issn pub-type="ppub">0034-7418</issn>
			<publisher>
				<publisher-name>Departamento de Farmácia, Facultad de Ciencias, Universidade Nacional da Colombia</publisher-name>
			</publisher>
		</journal-meta>
		<article-meta>
			<article-id pub-id-type="doi">10.15446/rcciquifa.v47n2.73933</article-id>
			<article-categories>
				<subj-group subj-group-type="heading">
					<subject>Artículos de Investigación Científica</subject>
				</subj-group>
			</article-categories>
			<title-group>
				<article-title>Preferential solvation of tricin in {ethanol (1) + water (2)} mixtures at several temperatures</article-title>
				<trans-title-group xml:lang="es">
					<trans-title>Solvatación preferencial de tricin en mezclas etanol + agua a varias temperaturas</trans-title>
				</trans-title-group>
			</title-group>
			<contrib-group>
				<contrib contrib-type="author">
					<name>
						<surname>Sandoval-Castro</surname>
						<given-names>Juan José</given-names>
					</name>
					<xref ref-type="aff" rid="aff1"><sup>1</sup></xref>
				</contrib>
				<contrib contrib-type="author">
					<name>
						<surname>Ortiz</surname>
						<given-names>Claudia Patricia</given-names>
					</name>
					<xref ref-type="aff" rid="aff2"><sup>2</sup></xref>
				</contrib>
				<contrib contrib-type="author">
					<name>
						<surname>Rodríguez-Rubiano</surname>
						<given-names>Juan Diego</given-names>
					</name>
					<xref ref-type="aff" rid="aff3"><sup>3</sup></xref>
				</contrib>
				<contrib contrib-type="author">
					<name>
						<surname>Rodríguez-Rodríguez</surname>
						<given-names>Gerson Andrés</given-names>
					</name>
					<xref ref-type="aff" rid="aff4"><sup>4</sup></xref>
				</contrib>
				<contrib contrib-type="author">
					<name>
						<surname>Delgado</surname>
						<given-names>Daniel Ricardo</given-names>
					</name>
					<xref ref-type="aff" rid="aff1"><sup>1</sup></xref>
					<xref ref-type="corresp" rid="c1"><sup>*</sup></xref>
				</contrib>
			</contrib-group>
			<aff id="aff1">
				<label>1</label>
				<institution content-type="original"> Grupo de Investigaciones GRIAUCC, Programa de Ingeniería Industrial, Facultad de Ingeniería, Universidad Cooperativa de Colombia, Neiva, Colombia, calle 11 No. 1-51, Neiva Huila, Colombia.</institution>
				<institution content-type="normalized">Universidad Cooperativa de Colombia</institution>
				<institution content-type="orgdiv2">Grupo de Investigaciones GRIAUCC, Programa de Ingeniería Industrial</institution>
				<institution content-type="orgdiv1">Facultad de Ingeniería</institution>
				<institution content-type="orgname">Universidad Cooperativa de Colombia</institution>
				<addr-line>
					<city>Neiva</city>
				</addr-line>
				<country country="CO">Colombia</country>
			</aff>
			<aff id="aff2">
				<label>2</label>
				<institution content-type="original"> Grupo de Investigaciones en Seguridad y Salud en el Trabajo - FET, Programa de Administración de la Salud Ocupacional, Fundación Escuela Tecnológica de Neiva, Km. 11 vía al Sur, Neiva-Rivera, Colombia.</institution>
				<institution content-type="orgdiv2">Grupo de Investigaciones en Seguridad y Salud en el Trabajo - FET</institution>
				<institution content-type="orgdiv1">Programa de Administración de la Salud Ocupacional</institution>
				<institution content-type="orgname">Fundación Escuela Tecnológica de Neiva</institution>
				<addr-line>
					<city>Neiva</city>
				</addr-line>
				<country country="CO">Colombia</country>
			</aff>
			<aff id="aff3">
				<label>3</label>
				<institution content-type="original"> Programa de Ingeniería Industrial, Facultad de Ingeniería, Universidad Antonio Nariño, sede Buganviles, calle 19 No. 42-98, Neiva Huila, Colombia.</institution>
				<institution content-type="normalized">Universidad Antonio Nariño</institution>
				<institution content-type="orgdiv2">Programa de Ingeniería Industrial</institution>
				<institution content-type="orgdiv1">Facultad de Ingeniería</institution>
				<institution content-type="orgname">Universidad Antonio Nariño</institution>
				<addr-line>
					<city>Neiva</city>
					<state>Huila</state>
				</addr-line>
				<country country="CO">Colombia</country>
			</aff>
			<aff id="aff4">
				<label>4</label>
				<institution content-type="original"> Grupo de Investigaciones Farmacéutico-Fisicoquímicas, Departamento de Farmacia, Facultad de Ciencias, Universidad Nacional de Colombia, sede Bogotá, Cra. 30 No. 45-03, Bogotá, D. C., Colombia.</institution>
				<institution content-type="normalized">Universidad Nacional de Colombia</institution>
				<institution content-type="orgdiv2">Grupo de Investigaciones Farmacéutico-Fisicoquímicas, Departamento de Farmacia</institution>
				<institution content-type="orgdiv1">Facultad de Ciencias</institution>
				<institution content-type="orgname">Universidad Nacional de Colombia</institution>
				<addr-line>
					<city>Bogotá</city>
					<state>D. C</state>
				</addr-line>
				<country country="CO">Colombia</country>
			</aff>
			<author-notes>
				<corresp id="c1">
					<label><sup>*</sup></label> E-mail: <email>danielr.delgado@campusucc.edu.co</email>.</corresp>
			</author-notes>
			<pub-date pub-type="epub-ppub">
				<season>May-Aug</season>
				<year>2018</year>
			</pub-date>
			<volume>47</volume>
			<issue>2</issue>
			<fpage>135</fpage>
			<lpage>148</lpage>
			<history>
				<date date-type="received">
					<day>22</day>
					<month>01</month>
					<year>2018</year>
				</date>
				<date date-type="accepted">
					<day>23</day>
					<month>02</month>
					<year>2018</year>
				</date>
			</history>
			<permissions>
				<license license-type="open-access" xlink:href="https://creativecommons.org/licenses/by/4.0/" xml:lang="en">
					<license-p>This is an open-access article distributed under the terms of the Creative Commons Attribution License</license-p>
				</license>
			</permissions>
			<abstract>
				<title>SUMMARY</title>
				<p>The preferential solvation parameters of tricin in {ethanol (1) + water (2)} binary mixtures were obtained from their thermodynamic properties by means of the inverse Kirkwood-Buff integrals method. Tricin is very sensitive to specific solvation effects, so the preferential solvation parameter by ethanol (1), <italic>δx</italic>
 <sub>1,3</sub> is negative in the water-rich mixtures but positive in all the other compositions at temperatures from 293.15, to 313.15 K. It is conjecturable that in water-rich mixtures the hydrophobic hydration around the aromatic and methyl groups of the drug plays a relevant role in the solvation. The higher drug solvation by ethanol in mixtures of similar solvent proportions and in ethanol-rich mixtures could be due mainly to polarity effects. In these mixtures, the drug would be acting as Lewis acid with the ethanol molecules because this co-solvent is more basic than water.</p>
			</abstract>
			<trans-abstract xml:lang="es">
				<title>RESUMEN</title>
				<p>Los parámetros de solvatación preferencial del tricina en mezclas {etanol (1) + agua (2)} se obtuvieron a partir de las propiedades termodinámicas de solución, mediante el método de las integrales inversas de Kirkwood-Buff. La tricina es muy sensible a los efectos de solvatación específicos, por lo que el parámetro de solvatación preferencial, <italic>δx</italic>
 <sub>1,3</sub> es negativo en las mezclas ricas en agua, pero positivo en todas las otras composiciones a temperaturas desde 293,15 hasta 313,15 K. Se puede establecer que en mezclas ricas en agua la hidratación hidrofóbica alrededor de los grupos aromáticos y metilo del fármaco tiene un papel relevante en la solvatación. La mayor solvatación del fármaco por etanol se presenta en mezclas de proporción intermedia y en mezclas ricas en etanol, esto podría deberse principalmente a los efectos de la polaridad. En estas mezclas, el fármaco actuaría como ácido de Lewis con las moléculas de etanol, puesto que este codisolvente es más básico que el agua.</p>
			</trans-abstract>
			<kwd-group xml:lang="en">
				<title><italic>Key words:</italic></title>
				<kwd>Tricin</kwd>
				<kwd>IKBI</kwd>
				<kwd>ethanol</kwd>
				<kwd>preferential solvation</kwd>
			</kwd-group>
			<kwd-group xml:lang="es">
				<title><italic>Palabras clave:</italic></title>
				<kwd>Tricina</kwd>
				<kwd>IKBI</kwd>
				<kwd>etanol</kwd>
				<kwd>solvatación preferencial</kwd>
			</kwd-group>
			<counts>
				<fig-count count="4"/>
				<table-count count="4"/>
				<equation-count count="9"/>
				<ref-count count="44"/>
				<page-count count="14"/>
			</counts>
		</article-meta>
	</front>
	<body>
		<sec sec-type="intro">
			<title>INTRODUCTION</title>
			<p>Tricin (5,7-dihydroxy-2-(4-hydroxy-3,5-dimethoxyphenyl)chromen-4-one) (<xref ref-type="fig" rid="f1">Figure 1</xref>) is a flavone often found in the outer layer of cereal crops, has also been associated with reduction in cancer. In a mouse model of intestinal cancer, addition of tricin to the diet (0.2%, which was about 6 mg per mouse per day) resulted in 33% fewer intestinal adenomas <sup>[</sup><xref ref-type="bibr" rid="B1"><sup>1</sup></xref><sup>].</sup> In another study, dietary tricin was found to inhibit inflammation-induced colon cancer in mice <sup>[</sup><xref ref-type="bibr" rid="B2"><sup>2</sup></xref><sup>].</sup> Additional beneficial health effects of tricin are summarized in a recent review <sup>[</sup><xref ref-type="bibr" rid="B3"><sup>3</sup></xref><sup>]</sup>.</p>
			<p>
				<fig id="f1">
					<label>Figure 1</label>
					<caption>
						<title>Molecular structure of tricin.</title>
					</caption>
					<graphic xlink:href="0034-7418-rccqf-47-02-135-gf1.gif"/>
				</fig>
			</p>
			<p>In foods tricin is mainly found in whole cereal grains, such as rice, barley, oat, and wheat, also, in medicinal plants such as <italic>Artemisia copa</italic> 
 <sup>[</sup><xref ref-type="bibr" rid="B4"><sup>4</sup></xref><sup>]</sup>. However, higher levels of tricin and its derivatives are often found in other nonedible tissues, such as leaves and grain hulls. Because of the potential therapeutic use of tricin and its derivatives, extraction from such nonedible sources has been proposed <sup>[</sup><xref ref-type="bibr" rid="B5"><sup>5</sup></xref><sup>]</sup>. Tricin has also recently been found as a component of lignin in some species, particularly monocots <sup>[</sup><xref ref-type="bibr" rid="B6"><sup>6</sup></xref><sup>]</sup>.</p>
			<p>Within the context of this article, the studies of the solubility of drugs in solvent mixtures have as their purpose the modeling of the solubilities, with the aim of reducing the number of experimental tests, and in the best case, to bring them to zero <sup>[</sup><xref ref-type="bibr" rid="B7"><sup>7</sup></xref><sup>-</sup><xref ref-type="bibr" rid="B12"><sup>12</sup></xref><sup>]</sup>. Cheng <italic>et al.</italic> 
 <sup>[</sup><xref ref-type="bibr" rid="B13"><sup>13</sup></xref><sup>]</sup> determined the solubility of Tricin in {ethanol (1) + water (2)} cosolvent mixtures at diferent temperatures. Some thermodynamic functions associated to the dissolution of this drug were obtained, but nothing about the drug is preferentially solvated by water and by ethanol in the aqueous solvent mixtures. Nevertheless, more insight into the interactions of the drug molecules with those of the components of the mixed solvent would help in the choice of better co-solvents for the enhancement of drug solubilities in aqueous media <sup>[</sup><xref ref-type="bibr" rid="B14"><sup>14</sup></xref><sup>-</sup><xref ref-type="bibr" rid="B16"><sup>16</sup></xref><sup>]</sup>.</p>
			<p>The professor Marcus addressed this problem by means the inverse Kirkwood-Buff integral (IKBI) method <sup>[</sup><xref ref-type="bibr" rid="B17"><sup>17</sup></xref><sup>,</sup><xref ref-type="bibr" rid="B18"><sup>18</sup></xref><sup>]</sup>. Where the results are expressed in terms of the preferential solvation parameter δx<sup>3,1</sup> for the solute tricin (3) by the component solvents ethanol (1) and water 82):</p>
			<p>
				<disp-formula id="e1">
					<graphic xlink:href="0034-7418-rccqf-47-02-135-e1.gif"/>
				</disp-formula>
			</p>
			<p>where (δx<sub>3,1</sub> is the local mole fraction of 1 in the surroundings of the solute 3 and x<sub>1</sub> is its mole fraction in the bulk solvent mixture. 3 is preferentially solvated by 1 when (δx<sub>3,1</sub>&gt; 0, otherwise by 2. Negligible preferential solvation is indicated when | (δx<sub>3,1</sub>| ≤ 0.01, but values δx<sub>3,1</sub>
 <italic>≈ x</italic>
 <sub>
 <italic>2</italic>
</sub> signify δx<sub>3,1</sub>
 <italic>≈</italic> 1 or complete selective solvation of 3 by 1. The magnitude and shape of the (δx<sub>3,1</sub>= <italic>f</italic> (<italic>x</italic>
 <sub>1</sub>) curve provide the desired information on the relative strength of the interactions of 3 with 1 and with 2 in their mixture.</p>
			<p>In order to apply the IKBI method, the solubility data need to be transformed into standard molar Gibbs energies of transfer from one of the components, say 2, into the mixture 1+2. If x<sub>2</sub> is the solubility as a function of the solvent composition, then:</p>
			<p>
				<disp-formula id="e2">
					<graphic xlink:href="0034-7418-rccqf-47-02-135-e2.gif"/>
				</disp-formula>
			</p>
			<sec>
				<title>Theoretical</title>
			</sec>
			<sec>
				<title>Preferential solvation</title>
				<p>The IKBI approach depends on obtaining the Kirkwood-Buff integrals as follows <sup>[</sup><xref ref-type="bibr" rid="B17"><sup>17</sup></xref><sup>-</sup><xref ref-type="bibr" rid="B22"><sup>22</sup></xref><sup>]</sup></p>
				<p>
					<disp-formula id="e3">
						<graphic xlink:href="0034-7418-rccqf-47-02-135-e3.gif"/>
					</disp-formula>
				</p>
				<p>Here <italic>G</italic>
 <sub>
 <italic>1,3</italic>
</sub> and <italic>G</italic>
 <sub>
 <italic>2,3</italic>
</sub> are the Kirkwood-Buff integrals (in cm<sup>3</sup> mol<sup>-1</sup>) as obtained from the thermodynamic data: the isothermal compressibility of the solvent mixtures, <italic>κ</italic>
 <sub>
 <italic>τ</italic>
</sub> (in GPa<sup>-1</sup>), and standard partial molar volume of solute in this mixture, V<sub>3</sub> (in cm<sup>3</sup> mol<sup>-1</sup>). The functions.</p>
				<p><italic>D</italic> and <italic>Q</italic> (in kJ mol<sup>-1</sup>, as is <italic>RT)</italic> are given in equations (5) and (6), and depend on the first derivative of standard molar Gibbs energies of transfer, ∆<sub>tr</sub>
 <italic>G</italic>
 <sup>o</sup>, and the second derivative of the excess Gibbs energy of mixing of the two solvents, <italic>G</italic>
 <sup>
 <italic>E</italic>
</sup> 
 <sub>
 <italic>1+2</italic>
</sub> , with respect to the composition <sup>[</sup><xref ref-type="bibr" rid="B23"><sup>23</sup></xref><sup>,</sup><xref ref-type="bibr" rid="B24"><sup>24</sup></xref><sup>]</sup>.</p>
				<p>
					<disp-formula id="e4">
						<graphic xlink:href="0034-7418-rccqf-47-02-135-e4.gif"/>
					</disp-formula>
				</p>
				<p>A final quantity that is required is the correlation volume around 3, <italic>V</italic>
 <sub>
 <italic>œr</italic>
</sub> 
 <italic>,</italic> within which preferential solvation takes place and the local mole fraction, x<sup>L</sup>
 <sub>1,3</sub>, is defined <sup>[</sup><xref ref-type="bibr" rid="B18"><sup>18</sup></xref><sup>,</sup><xref ref-type="bibr" rid="B25"><sup>25</sup></xref><sup>]</sup>.</p>
				<p>
					<disp-formula id="e5">
						<graphic xlink:href="0034-7418-rccqf-47-02-135-e5.gif"/>
					</disp-formula>
				</p>
				<p>This volume involves one solvation shell and depends on the size of the solute molecule (its radius, r<sub>3</sub> in nm, equation 8) plus a distance of one mean solvent diameter from the surface of the solute.</p>
				<p>
					<disp-formula id="e6">
						<graphic xlink:href="0034-7418-rccqf-47-02-135-e6.gif"/>
					</disp-formula>
				</p>
				<p><italic>The</italic> resulting correlation volume, in cm<sup>3</sup> mol<sup>-1</sup>, the numerical coefficients of which relate sizes to volumes, requires iteration, since it involves the local mole fractions of the two solvents.</p>
				<p>Finally, the resulting preferential solvation parameter is then:</p>
				<p>
					<disp-formula id="e7">
						<graphic xlink:href="0034-7418-rccqf-47-02-135-e7.gif"/>
					</disp-formula>
				</p>
				<p>However, the correlation volume requires iteration, because it depends on the local mole fractions <sup>[</sup><xref ref-type="bibr" rid="B19"><sup>19</sup></xref><sup>,</sup><xref ref-type="bibr" rid="B26"><sup>26</sup></xref><sup>,</sup><xref ref-type="bibr" rid="B27"><sup>27</sup></xref><sup>]</sup>.</p>
			</sec>
		</sec>
		<sec sec-type="results|discussion">
			<title>RESULTS AND DISCUSSION</title>
			<p><italic>The</italic> experimental solubility of tricin (3) in {ethanol (1) + water (2)} mixtures (<xref ref-type="fig" rid="f2">Fig. 2</xref>) was taken from the literature <sup>[</sup><xref ref-type="bibr" rid="B13"><sup>13</sup></xref><sup>]</sup>.</p>
			<p>
				<fig id="f2">
					<label>Figure 2</label>
					<caption>
						<title>Experimental molar solubility of Tricin in {ethanol (1) + water (2)} mixtures at different temperatures; (■=293.15 K; ●=298.15 K; ▲=303.15 K; 4=308.15 K; ♦= 313.15 K). Data taken from Cheng <italic>et al.</italic> (2016) <sup>[</sup><xref ref-type="bibr" rid="B6"><sup>6</sup></xref><sup>]</sup>. (10<sup>6</sup> x<sub>3</sub>).</title>
					</caption>
					<graphic xlink:href="0034-7418-rccqf-47-02-135-gf2.gif"/>
				</fig>
			</p>
			<p>The solubility increases with temperature in all cases indicating that the dissolution process is endothermic. The highest solubility of tricin (3) expressed as a mole fraction were obtained in near ethanol (1) at <italic>T</italic> = 313.15 K, whereas the lowest values were found in pure water (2) at 293.15 K (<xref ref-type="fig" rid="f2">Figure 2</xref>).</p>
			<p>On the other hand, <xref ref-type="fig" rid="f2">Fig. 2</xref> depict the solubility profiles as a function of the polarity of the mixtures, expressed by their solubility parameters (<italic>δ</italic>
 <sub>mix</sub>). For a binary mixture <italic>δ</italic>
 <sub>mix</sub> is calculated from the solubility parameters of the pure solvents (<italic>δ</italic>
 <sub>1</sub> = 26.5 MPa<sup>1/2</sup> and <italic>δ</italic>
 <sub>2</sub> = 47.9 MPa<sup>1/2 [</sup><xref ref-type="bibr" rid="B28"><sup>28</sup></xref><sup>,</sup><xref ref-type="bibr" rid="B29"><sup>29</sup></xref><sup>]</sup>).</p>
			<p>The solubility parameter of solute, estimated according to the groups contribution method proposed by Fedors <sup>[</sup><xref ref-type="bibr" rid="B21"><sup>21</sup></xref><sup>]</sup>, is <italic>δ</italic>
 <sub>
 <italic>3</italic>
</sub> = 34.44 MPa<sup>1/2</sup> (<xref ref-type="table" rid="t1">Table 1</xref>). Usually, the maximum solubility of a substance is found in a solvent or mixture of solvents with polarity similar to that of the solute. Tis behavior has been described by Delgado and Martinez in several investigations <sup>[</sup><xref ref-type="bibr" rid="B30"><sup>30</sup></xref><sup>-</sup><xref ref-type="bibr" rid="B37"><sup>37</sup></xref><sup>]</sup>. However, the experimental data did not present a maximum in a mixture but in pure ethanol (1).</p>
			<p>
				<table-wrap id="t1">
					<label>Table 1</label>
					<caption>
						<title>Application ofthe Fedors' method to estimate internal energy, molar volume, and Hildebrand solubility parameter of Tricin (3).</title>
					</caption>
					<graphic xlink:href="0034-7418-rccqf-47-02-135-gt1.gif"/>
				</table-wrap>
			</p>
			<sec>
				<title>Preferential solvation</title>
				<p>Standard molar Gibbs energy of transfer of tricin from neat water to {ethanol (1) + water (2)} mixtures is calculated and correlated to a non-regular polynomial from the drug solubility data by using equation (10). <xref ref-type="fig" rid="f3">Figure 3</xref> shows the Gibbs energy of transfer behavior at 323.15 K. Tus, the coefficients of the polynomials are shown in <xref ref-type="table" rid="t2">Table 2</xref>.</p>
				<p>
					<disp-formula id="e8">
						<graphic xlink:href="0034-7418-rccqf-47-02-135-e8.gif"/>
					</disp-formula>
				</p>
				<p>
					<table-wrap id="t2">
						<label>Table 2</label>
						<caption>
							<title>Coefficients of the equation (10) applied to the Gibbs energy of transfer of tricin (3) from neat water (2) to {ethanol (1) + water (2)} mixtures at several temperatures.</title>
						</caption>
						<graphic xlink:href="0034-7418-rccqf-47-02-135-gt2.gif"/>
					</table-wrap>
				</p>
				<p>
					<fig id="f3">
						<label>Figure 3</label>
						<caption>
							<title>Gibbs energy of transfer of tricin (3) from neat water (2) to {ethanol (1) + water (2)} co-solvent mixtures at some temperatures (●=293.15 K; ◊=303.15 K; Δ=313.15 K).</title>
						</caption>
						<graphic xlink:href="0034-7418-rccqf-47-02-135-gf3.gif"/>
					</fig>
				</p>
				<p><italic>Thus D</italic> values are calculated from the first derivative of polynomial models (Equation 11) solved according to the co-solvent mixtures composition. <italic>This</italic> procedure was done varying by 0.05 in mole fraction of methanol but in the following tables the respective values are reported varying only by 0.10.</p>
				<p>
					<disp-formula id="e9">
						<graphic xlink:href="0034-7418-rccqf-47-02-135-e9.gif"/>
					</disp-formula>
				</p>
				<p><italic>Q</italic> and <italic>RT κ</italic>
 <sub>
 <italic>τ</italic>
</sub> values for {ethanol (1) + water (2)} binary mixtures, as well as the partial molar volumes of ethanol (1) and water (2), at the three temperatures considered here, were taken from the literature <sup>[</sup><xref ref-type="bibr" rid="B22"><sup>22</sup></xref><sup>,</sup><xref ref-type="bibr" rid="B38"><sup>38</sup></xref><sup>,</sup><xref ref-type="bibr" rid="B39"><sup>39</sup></xref><sup>]</sup>.</p>
				<p>Otherwise, partial molar volumes of nonelectrolyte drugs are not frequently reported in the literature. This is because of the large uncertainty obtained in its determination due to their low solubilities, in particular in aqueous media. For this reason, in the first approach, the molar volume of tricin was considered as independent of co-solvent composition and temperature, as they are calculated according to the groups contribution method proposed by Fedors <sup>[</sup><xref ref-type="bibr" rid="B29"><sup>29</sup></xref><sup>]</sup>. On the other hand, the radius of the drug molecule was calculated by using equation 8, as r<sub>3</sub> = 0.407 nm.</p>
				<p>In order to apply the IKBI method, the correlation volume was iterated three times by using the equations (1), (7) and (9) to obtain the final values reported in <xref ref-type="table" rid="t3">Table 3</xref>. This property is almost independent on temperature in water-rich mixtures but increases to some extent in ethanol-rich mixtures. This would be expectable according to the variation of the respective molar expansibilities with the mixtures composition <sup>[</sup><xref ref-type="bibr" rid="B40"><sup>40</sup></xref><sup>]</sup>.</p>
				<p>
					<table-wrap id="t3">
						<label>Table 3</label>
						<caption>
							<title>Correlation volume (cm<sup>3</sup> mol<sup>-1</sup>) for tricin in {ethanol (1) + water (2)} co-solvent mixtures at several temperatures after three iterations.</title>
						</caption>
						<table>
							<colgroup>
								<col/>
								<col/>
								<col/>
								<col/>
								<col/>
								<col/>
							</colgroup>
							<thead>
								<tr>
									<th align="center">X<sub>1</sub></th>
									<th align="left">293.15 K</th>
									<th align="left">298.15 K</th>
									<th align="left">303.15 K</th>
									<th align="left">308.15 K</th>
									<th align="left">313.15 K</th>
								</tr>
							</thead>
							<tbody>
								<tr>
									<td align="left">0.00</td>
									<td align="left">790.74</td>
									<td align="left">791.26</td>
									<td align="left">791.60</td>
									<td align="left">792.09</td>
									<td align="left">792.87</td>
								</tr>
								<tr>
									<td align="left">0.10</td>
									<td align="left">814.11</td>
									<td align="left">810.66</td>
									<td align="left">808.86</td>
									<td align="left">812.33</td>
									<td align="left">813.15</td>
								</tr>
								<tr>
									<td align="left">0.20</td>
									<td align="left">938.40</td>
									<td align="left">939.33</td>
									<td align="left">941.50</td>
									<td align="left">944.50</td>
									<td align="left">946.85</td>
								</tr>
								<tr>
									<td align="left">0.30</td>
									<td align="left">1033.69</td>
									<td align="left">1036.60</td>
									<td align="left">1039.18</td>
									<td align="left">1041.04</td>
									<td align="left">1043.50</td>
								</tr>
								<tr>
									<td align="left">0.40</td>
									<td align="left">1115.76</td>
									<td align="left">1118.16</td>
									<td align="left">1119.75</td>
									<td align="left">1122.04</td>
									<td align="left">1124.45</td>
								</tr>
								<tr>
									<td align="left">0.50</td>
									<td align="left">1196.96</td>
									<td align="left">1197.75</td>
									<td align="left">1198.42</td>
									<td align="left">1202.63</td>
									<td align="left">1205.53</td>
								</tr>
								<tr>
									<td align="left">0.60</td>
									<td align="left">1281.26</td>
									<td align="left">1280.71</td>
									<td align="left">1281.36</td>
									<td align="left">1288.19</td>
									<td align="left">1292.30</td>
								</tr>
								<tr>
									<td align="left">0.70</td>
									<td align="left">1363.04</td>
									<td align="left">1364.41</td>
									<td align="left">1367.61</td>
									<td align="left">1376.55</td>
									<td align="left">1383.36</td>
								</tr>
								<tr>
									<td align="left">0.80</td>
									<td align="left">1428.86</td>
									<td align="left">1435.71</td>
									<td align="left">1443.43</td>
									<td align="left">1451.91</td>
									<td align="left">1462.05</td>
								</tr>
								<tr>
									<td align="left">0.90</td>
									<td align="left">1485.75</td>
									<td align="left">1493.95</td>
									<td align="left">1501.84</td>
									<td align="left">1507.52</td>
									<td align="left">1516.46</td>
								</tr>
								<tr>
									<td align="left">1.00</td>
									<td align="left">1560.82</td>
									<td align="left">1566.06</td>
									<td align="left">1571.22</td>
									<td align="left">1576.68</td>
									<td align="left">1582.68</td>
								</tr>
							</tbody>
						</table>
						<table-wrap-foot>
							<fn id="TFN1">
								<p>The preferential solvation parameter, <italic>δx</italic>
 <sub>
 <italic>1,3</italic>
</sub> for ethanol (1) around tricin (3) is displayed in <xref ref-type="fig" rid="f4">Fig. 4</xref> at five temperatures. The values of <italic>δx</italic>
 <sub>
 <italic>13</italic>
</sub> vary non-linearly with the proportion of ethanol (1) in the alcoholic mixtures (<xref ref-type="fig" rid="f4">figure 4</xref>). The addition of ethanol to water causes a negative change in <italic>δx</italic>
 <sub>1,3</sub> from pure water (2) up to the 0.20 in molar fraction of ethanol (1) reaching minimum values near to -0.08 at 0.05 in molar fraction of ethanol at 303.15 K. In this composition, water is preferred over ethanol around the tricin (3), this because possibly the structuring of water molecules around the non-polar groups of this drug leading to hydrophobic hydration of the aromatic and methyl groups (<xref ref-type="fig" rid="f1">Fig.1</xref>), contributes to lowering of the net <italic>δx</italic>
 <sub>
 <italic>1,3</italic>
</sub> to negative values in these water-rich mixtures. This behavior is observed at all study temperatures as can be seen in <xref ref-type="table" rid="t4">Table 4</xref>. Although, a clear influence of the temperature in water-rich mixtures is not perceived, in ethanol-rich mixtures the solvation by ethanol increases with the increase in temperature what matches the solubility profile.</p>
							</fn>
						</table-wrap-foot>
					</table-wrap>
				</p>
				<p>
					<fig id="f4">
						<label>Figure 4</label>
						<caption>
							<title><italic>δx</italic>
 <sub>1,3</sub> values tricin (3) in {ethanol (1) + water (2)} co-solvent mixtures at several temperatures. (●=293.15 K; ▲=298.15 K; □=303.15 K; ◊=308.15 Δ; =313.15 K).</title>
						</caption>
						<graphic xlink:href="0034-7418-rccqf-47-02-135-gf4.gif"/>
					</fig>
				</p>
				<p>
					<table-wrap id="t4">
						<label>Table 4</label>
						<caption>
							<title><italic>δ</italic>x<sub>1,3</sub>, values of tricin (3) in {ethanol (1) + water (2)} co-solvent mixtures at several temperatures.</title>
						</caption>
						<table>
							<colgroup>
								<col/>
								<col/>
								<col/>
								<col/>
								<col/>
								<col/>
							</colgroup>
							<thead>
								<tr>
									<th align="center"><italic>X</italic>
 <sub>
 <italic>1</italic>
</sub></th>
									<th align="left">293.15 K</th>
									<th align="left">298.15 K</th>
									<th align="left">303.15 K</th>
									<th align="left">308.15 K</th>
									<th align="left">313.15 K</th>
								</tr>
							</thead>
							<tbody>
								<tr>
									<td align="left">0.00</td>
									<td align="left">0.000</td>
									<td align="left">0.000</td>
									<td align="left">0.000</td>
									<td align="left">0.000</td>
									<td align="left">0.000</td>
								</tr>
								<tr>
									<td align="left">0.10</td>
									<td align="left">-0.070</td>
									<td align="left">-0.075</td>
									<td align="left">-0.078</td>
									<td align="left">-0.075</td>
									<td align="left">-0.075</td>
								</tr>
								<tr>
									<td align="left">0.20</td>
									<td align="left">-0.012</td>
									<td align="left">-0.013</td>
									<td align="left">-0.013</td>
									<td align="left">-0.012</td>
									<td align="left">-0.012</td>
								</tr>
								<tr>
									<td align="left">0.30</td>
									<td align="left">0.010</td>
									<td align="left">0.011</td>
									<td align="left">0.010</td>
									<td align="left">0.009</td>
									<td align="left">0.009</td>
								</tr>
								<tr>
									<td align="left">0.40</td>
									<td align="left">0.016</td>
									<td align="left">0.015</td>
									<td align="left">0.013</td>
									<td align="left">0.012</td>
									<td align="left">0.011</td>
								</tr>
								<tr>
									<td align="left">0.50</td>
									<td align="left">0.022</td>
									<td align="left">0.019</td>
									<td align="left">0.015</td>
									<td align="left">0.016</td>
									<td align="left">0.015</td>
								</tr>
								<tr>
									<td align="left">0.60</td>
									<td align="left">0.034</td>
									<td align="left">0.027</td>
									<td align="left">0.023</td>
									<td align="left">0.028</td>
									<td align="left">0.027</td>
								</tr>
								<tr>
									<td align="left">0.70</td>
									<td align="left">0.043</td>
									<td align="left">0.038</td>
									<td align="left">0.037</td>
									<td align="left">0.044</td>
									<td align="left">0.046</td>
								</tr>
								<tr>
									<td align="left">0.80</td>
									<td align="left">0.032</td>
									<td align="left">0.034</td>
									<td align="left">0.039</td>
									<td align="left">0.044</td>
									<td align="left">0.051</td>
								</tr>
								<tr>
									<td align="left">0.90</td>
									<td align="left">0.009</td>
									<td align="left">0.014</td>
									<td align="left">0.018</td>
									<td align="left">0.019</td>
									<td align="left">0.023</td>
								</tr>
								<tr>
									<td align="left">1.00</td>
									<td align="left">0.000</td>
									<td align="left">0.000</td>
									<td align="left">0.000</td>
									<td align="left">0.000</td>
									<td align="left">0.000</td>
								</tr>
							</tbody>
						</table>
					</table-wrap>
				</p>
				<p>In the mixtures with composition 0.25 &lt; x<sub>1</sub> &lt; 1.00, the local mole fraction of ethanol is greater than the one in the bulk and it increases with the temperature increasing. In this way, the co-solvent action may be related to the breaking of the ordered structure of water (hydrogen bonds) around the nonpolar moieties of the drug which increases the solvation of the tricin and has a maximum value near to x<sub>1</sub> = 0.75, i.e. (<italic>δx</italic>
 <sub>1,3</sub> = 0.052. On the other hand, although, as mentioned above, the maximum solubility was not achieved in a cosolvent mixture, whit would be expected theoretically, the maximum solvation is achieved in mixtures with polarities similar to those of tricin (3), this factor could also be involved in these behaviors.</p>
				<p>The tricin (3) could act in solution as Lewis acids due to the hydrogen atom in their -OH groups in order to establish hydrogen bonds with proton-acceptor functional groups in EtOH and water (oxygen atom in -OH). In addition, these drugs could act as Lewis bases due to free electron pairs in oxygen atoms of hydroxyl and alkoxy groups to interact with hydrogen atoms present in both solvents. In this context, tricin has three hydrogen-bonding donor and seven hydrogen-bonding acceptor groups.</p>
				<p>According to the preferential solvation results, it is conjecturable that in intermediate composition mixtures and ethanol-rich mixtures, tricin (3) is acting as Lewis acids with the ethanol molecules because this co-solvent is more basic than water as indicated by the Kamlet-Taft hydrogen bond acceptor parameters (<italic>β</italic>), i.e. 0.75 for ethanol (1) and 0.47 for water (2) <sup>[</sup><xref ref-type="bibr" rid="B41"><sup>41</sup></xref><sup>,</sup><xref ref-type="bibr" rid="B42"><sup>42</sup></xref><sup>]</sup>. In this way, tricin would prefer ethanol (1) instead of water. This behavior is similar to that presented by other drugs in aqueous cosolvent systems <sup>[</sup><xref ref-type="bibr" rid="B27"><sup>27</sup></xref><sup>,</sup><xref ref-type="bibr" rid="B43"><sup>43</sup></xref><sup>,</sup><xref ref-type="bibr" rid="B44"><sup>44</sup></xref><sup>]</sup>.</p>
			</sec>
		</sec>
		<sec sec-type="conclusions">
			<title>CONCLUSIONS</title>
			<p>Explicit expressions for local mole fraction of ethanol and water around of tricin were derived on the basis of the IKBI method applied to equilibrium solubility values of this drug in {ethanol (1) + water (2)} mixtures. According to the performed analyses, tricin is preferentially solvated by water (2) in water-rich mixtures but preferentially solvated by ethanol (1) in mixtures with intermediate composition and those rich in ethanol at all temperatures considered.</p>
		</sec>
	</body>
	<back>
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		<fn-group>
			<fn fn-type="other" id="fn1">
				<label>DISCLOSURE STATEMENT</label>
				<p> No potential conflict of interest was reported by the authors.</p>
			</fn>
		</fn-group>
		<fn-group>
			<fn fn-type="other" id="fn2">
				<label>HOW TO CITE THIS ARTICLE</label>
				<p> J.J. Sandoval-Castro, C.P. Ortiz, J.D. Rodríguez-Rubiano, G.A. Rodríguez-Rodríguez, D.R. Delgado, Preferential solvation of tricin in {ethanol (1) + water (2)} mixtures at several temperatures, <italic>Rev. Colomb. Cienc. Quím. Farm.,</italic> 
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			</fn>
		</fn-group>
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</article>