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	<front>
		<journal-meta>
			<journal-id journal-id-type="publisher-id">dyna</journal-id>
			<journal-title-group>
				<journal-title>DYNA</journal-title>
				<abbrev-journal-title abbrev-type="publisher">Dyna rev.fac.nac.minas</abbrev-journal-title>
			</journal-title-group>
			<issn pub-type="ppub">0012-7353</issn>
			<publisher>
				<publisher-name>Universidad Nacional de Colombia</publisher-name>
			</publisher>
		</journal-meta>
		<article-meta>
			<article-id pub-id-type="doi">10.15446/dyna.v85n207.72374</article-id>
			<article-categories>
				<subj-group subj-group-type="heading">
					<subject>Artículos</subject>
				</subj-group>
			</article-categories>
			<title-group>
				<article-title>Molecular toxicity of potential liquid membranes for lactic acid removal from fermentation broths using <italic>Lactobacillus casei</italic> ATCC 393</article-title>
				<trans-title-group xml:lang="es">
					<trans-title>Toxicidad molecular de membranas liquidas potenciales para la remoción de ácido láctico a partir de caldos de fermentación con <italic>Lactobacillus casei</italic> ATCC 393</trans-title>
				</trans-title-group>
			</title-group>
			<contrib-group>
				<contrib contrib-type="author">
					<name>
						<surname>Pérez</surname>
						<given-names>Alan D.</given-names>
					</name>
					<xref ref-type="aff" rid="aff1"><sup>
 <italic>a</italic>
</sup></xref>
				</contrib>
				<contrib contrib-type="author">
					<name>
						<surname>Rodríguez-Barona</surname>
						<given-names>Sneyder</given-names>
					</name>
					<xref ref-type="aff" rid="aff2"><sup>
 <italic>b</italic>
</sup></xref>
				</contrib>
				<contrib contrib-type="author">
					<name>
						<surname>Fontalvo</surname>
						<given-names>Javier</given-names>
					</name>
					<xref ref-type="aff" rid="aff1"><sup>
 <italic>a</italic>
</sup></xref>
				</contrib>
			</contrib-group>
			<aff id="aff1">
				<label>a</label>
				<institution content-type="original"> Grupo de Investigación en Aplicación de Nuevas Tecnologías, Laboratorio de Intensificación de Procesos y Sistemas Híbridos, Departamento de Ingeniería Química, Facultad de Ingeniería y Arquitectura, Universidad Nacional de Colombia, Sede Manizales, Manizales, Colombia. adpereza@unal.edu.co, jfontalvoa@unal.edu.co</institution>
				<institution content-type="normalized">Universidad Nacional de Colombia</institution>
				<institution content-type="orgdiv2">Departamento de Ingeniería Química</institution>
				<institution content-type="orgdiv1">Facultad de Ingeniería y Arquitectura</institution>
				<institution content-type="orgname">Universidad Nacional de Colombia</institution>
				<addr-line>
					<city>Manizales</city>
				</addr-line>
				<country country="CO">Colombia</country>
				<email>adpereza@unal.edu.co</email>
				<email>jfontalvoa@unal.edu.co</email>
			</aff>
			<aff id="aff2">
				<label>b</label>
				<institution content-type="original"> Grupo de Investigación en Bacterias Ácido Lácticas y sus Aplicaciones Biotecnológicas ­ Industriales, Laboratorio de Ciencias de Alimentos, Departamento de Ingeniería Química, Facultad de Ingeniería y Arquitectura, Universidad Nacional de Colombia - Sede Manizales, Manizales, Colombia. snrodriguezba@unal.edu.co</institution>
				<institution content-type="normalized">Universidad Nacional de Colombia</institution>
				<institution content-type="orgname">Universidad Nacional de Colombia</institution>
				<addr-line>
					<city>Manizales</city>
				</addr-line>
				<country country="CO">Colombia</country>
				<email>snrodriguezba@unal.edu.co</email>
			</aff>
			<pub-date pub-type="epub-ppub">
				<season>Oct-Dec</season>
				<year>2018</year>
			</pub-date>
			<volume>85</volume>
			<issue>207</issue>
			<fpage>360</fpage>
			<lpage>366</lpage>
			<history>
				<date date-type="received">
					<day>23</day>
					<month>05</month>
					<year>2018</year>
				</date>
				<date date-type="rev-recd">
					<day>25</day>
					<month>11</month>
					<year>2018</year>
				</date>
				<date date-type="accepted">
					<day>04</day>
					<month>12</month>
					<year>2018</year>
				</date>
			</history>
			<permissions>
				<license license-type="open-access" xlink:href="https://creativecommons.org/licenses/by-nc-nd/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>Abstract</title>
				<p>Toxic effects of extractants and carriers of specific microorganisms must be taken into account before using them with hybrid fermentation processes that are combined with liquid membranes or liquid-liquid extraction. In the current research three extractants (trioctylamine, tri-iso-octylamine and Aliquat 336), three diluents (dodecane, dodecanol, and oleyl alcohol) and two mixtures (extractant/diluent) were tested for molecular toxicity on the bacteria <italic>Lactobacillus casei</italic> ATCC 393 as potential components of a liquid membrane or a liquid-liquid extraction process for lactic acid removal in an intensified fermentation process. Glucose consumption, lactic acid production, and cell growth were used as toxicity indicators. Physical properties of extractants and diluents were related to the molecular toxicity on the microorganism. These results show that mixtures of tri-iso-octylamine/dodecane and trioctylamine/dodecane at a proportion of 1:9 v/v have great potential to be used in liquid membranes or liquid-liquid extraction processes on hybrid fermentations with <italic>Lactobacillus casei</italic> ATCC 393.</p>
			</abstract>
			<trans-abstract xml:lang="es">
				<title>Resumen</title>
				<p>La toxicidad de extractantes y <italic>carriers</italic> sobre microrganismos específicos es clave a evaluar para implementar membranas líquidas o extracciones líquido-líquido integrados con fermentación. Se evaluó la toxicidad molecular de tres extractantes (trioctilamina, tri-iso-octilamina y Aliquat 336), tres diluyentes (dodecano, dodecanol y alcohol oleico) y dos mezclas (extractante/diluyente) sobre la bacteria <italic>Lactobacillus casei</italic> ATCC 393 como componentes potenciales de los procesos de separación mencionados para la remoción de ácido láctico en un proceso intensificado fermentativo. El consumo de glucosa, la producción de biomasa y de ácido láctico se usaron como indicadores de toxicidad. Las propiedades físicas de los extractantes y de los diluyentes fueron relacionadas con la toxicidad molecular sobre el microorganismo. De acuerdo a los resultados, las mezclas tri-iso-octilamina/dodecano y trioctilamina/dodecano a una proporción 1:9 v/v tienen gran potencial de ser usados en membranas líquidas o procesos de extracción líquido-líquido en fermentaciones híbridas con <italic>Lactobacillus casei</italic> ATCC 393.</p>
			</trans-abstract>
			<kwd-group xml:lang="en">
				<title><bold>
 <italic>Keywords</italic>:</bold></title>
				<kwd>process intensification</kwd>
				<kwd>liquid-liquid extraction</kwd>
				<kwd>trioctylamine</kwd>
				<kwd>tri-iso-octylamine</kwd>
				<kwd>Aliquat 336</kwd>
				<kwd>dodecane</kwd>
				<kwd>dodecanol</kwd>
				<kwd>oleyl alcohol</kwd>
			</kwd-group>
			<kwd-group xml:lang="es">
				<title><bold>
 <italic>Palabras clave</italic>:</bold></title>
				<kwd>intensificación de procesos</kwd>
				<kwd>extracción líquida</kwd>
				<kwd>trioctilanina</kwd>
				<kwd>tri-iso-octilamina</kwd>
				<kwd>Aliquat 336</kwd>
				<kwd>dodecano</kwd>
				<kwd>dodecanol</kwd>
				<kwd>alcohol oleico</kwd>
			</kwd-group>
			<counts>
				<fig-count count="6"/>
				<table-count count="1"/>
				<equation-count count="0"/>
				<ref-count count="37"/>
				<page-count count="7"/>
			</counts>
		</article-meta>
	</front>
	<body>
		<sec sec-type="intro">
			<title>1. Introduction</title>
			<p>Removal of organic acids through liquid membranes using tertiary amines has been the focus of several studies [<xref ref-type="bibr" rid="B1">1</xref>], especially for the recovery from fermentation systems. Succinic acid has been recovered using a hollow-fiber supported liquid membrane with a trialkylamine [<xref ref-type="bibr" rid="B2">2</xref>]. Citric acid has been removed using an emulsion liquid membrane with Alamine 336 [<xref ref-type="bibr" rid="B3">3</xref>]. Acetic acid has been separated by emulsion liquid membranes with Amberlite LA-2 (secondary amine), trioctylamine [<xref ref-type="bibr" rid="B4">4</xref>], and Aliquat 336 (quaternary ammonium salt) [<xref ref-type="bibr" rid="B5">5</xref>]. Lactic acid has been recovered by a supported liquid membrane with trioctylamine [<xref ref-type="bibr" rid="B6">6</xref>] and by emulsion liquid membranes with both tributyl phosphate and trioctylamine [<xref ref-type="bibr" rid="B7">7</xref>].</p>
			<p>In the aforementioned perstraction and reactive liquid-liquid extraction processes, an extractant or carrier is mixed with a diluent [<xref ref-type="bibr" rid="B1">1</xref>,<xref ref-type="bibr" rid="B4">4</xref>,<xref ref-type="bibr" rid="B8">8</xref>,<xref ref-type="bibr" rid="B9">9</xref>]. Several characteristics are required from these extractants and solvents, for instance: low viscosity, a high difference of densities with the aqueous phase (that contains the solute), low melting point, medium interfacial tension, high hydrophobicity, thermal stability, low price and availability [<xref ref-type="bibr" rid="B10">10</xref>-<xref ref-type="bibr" rid="B12">12</xref>], within others. Additionally, toxicity levels of extractant and diluent on microorganisms are key factors to take into account with liquid membranes or liquid-liquid extractions applied for the removal of metabolites from fermentation systems. </p>
			<p>Tertiary amines have commonly been used for organic acid removal owing to their high extraction availability, low water solubility and high selectivity [<xref ref-type="bibr" rid="B11">11</xref>,<xref ref-type="bibr" rid="B13">13</xref>-<xref ref-type="bibr" rid="B16">16</xref>] which is usually due to the formation of carboxylic acid-amine complexes [<xref ref-type="bibr" rid="B10">10</xref>,<xref ref-type="bibr" rid="B17">17</xref>]. Diluents allow for the adjustment of viscosity and density of the solvent phase [<xref ref-type="bibr" rid="B15">15</xref>], and on the other hand, provide high distribution coefficients [<xref ref-type="bibr" rid="B10">10</xref>]. Diluents can be inert or have an interaction with the extractant that influences its performance. An inert diluent can improve the physical extraction without affecting the transport mechanism [<xref ref-type="bibr" rid="B9">9</xref>] while an active diluent can have functional groups that interact with the carboxylic acid-amine complex solvating it in order to stabilize the complex [<xref ref-type="bibr" rid="B9">9</xref>,<xref ref-type="bibr" rid="B14">14</xref>].</p>
			<p>Toxic effects of a solvent on microorganisms are related with accumulation in the cytoplasmic cell membrane. At this level, modifications are made in the functionality of the membrane proteins. Solvents go into and disrupt the lipid bilayer. These compounds generate rupture and metabolite leakage damage. Its effect may result in cell lysis and death [<xref ref-type="bibr" rid="B18">18</xref>-<xref ref-type="bibr" rid="B20">20</xref>]. The aforementioned toxic effects have been related to a physical property of the substance, the logarithm of the partition coefficient of the solvent in an equimolar mixture of n-octanol and water (L<sub>og</sub> P<sub>ow</sub>) [<xref ref-type="bibr" rid="B18">18</xref>,<xref ref-type="bibr" rid="B21">21</xref>-<xref ref-type="bibr" rid="B23">23</xref>]. As lower the Log P<sub>ow</sub> is, the greater polarity and the toxicity of the solvent will be [<xref ref-type="bibr" rid="B22">22</xref>]. The solvent interacts with the microorganism mainly by two routes: direct contact between the cells and the solvent into the aqueous-organic interface (phase toxicity) and by the organic solvent that is soluble in the aqueous broth (molecular toxicity) [<xref ref-type="bibr" rid="B19">19</xref>,<xref ref-type="bibr" rid="B20">20</xref>,<xref ref-type="bibr" rid="B24">24</xref>,<xref ref-type="bibr" rid="B25">25</xref>].</p>
			<p>When a perstraction process is integrated with a fermentation process (hybrid process), the toxicity of the membrane phase (diluent/extractant) on the microorganisms can rise [<xref ref-type="bibr" rid="B10">10</xref>,<xref ref-type="bibr" rid="B16">16</xref>]. Thus, additional parameters have to be considered for designing the extraction or perstraction process including loading ratio, complexation equilibrium constant, stoichiometry and rate constant of the organic acid-amine complex [<xref ref-type="bibr" rid="B10">10</xref>,<xref ref-type="bibr" rid="B26">26</xref>]. In a hybrid process with in-situ product removal (ISPR) [<xref ref-type="bibr" rid="B27">27</xref>], either by reactive liquid-liquid extraction or supported liquid membranes, both molecular and phase toxicity affect cell growth and productivity. In order to reduce toxicity, filtration is used for removing biomass from the fermentation broth [<xref ref-type="bibr" rid="B25">25</xref>]. However, despite performing the product removal externally to the bioreactor, molecular toxicity can affect the microorganism. </p>
			<p>Toxicity of several solvents has been tested on different lactic acid microorganisms. For instance, toxicity of n-dodecane, paraffin oil, chloroform, 1,1,1-trichloroethane, carbon tetra-chloride, ethyl laurate, n-dodecanol, tri-n-dodecylamine, and perfluorodecalin were tested on <italic>Lactobacillus delbrueckii</italic> ATCC 9649 [<xref ref-type="bibr" rid="B28">28</xref>]. Also, the toxicity of Hostarex A327, trihexylphosphate, pentaphosphine-dipentylester, diisotridecylamine, n-octanol, isodecanol, isotridecanol, oleyl alcohol and n-alkanes (C10-C13) were measured on <italic>Rhizopus arrhizus</italic> CCM 8109 [<xref ref-type="bibr" rid="B29">29</xref>]. Toxic effects of Imidazolium-based ionic liquids were tested on <italic>Lactobacillus delbruekii</italic> NRIC 1683 [<xref ref-type="bibr" rid="B24">24</xref>]. Toxicity of Tributylphosphate, tridodecylamine, dioctylamine, tri-n-octylamine, Alamine 336, Aliquat 336, 1-octanol, 1-decanol, 1-dodecanol, oleyl alcohol, n-octane, n-decane, dodecane and kerosene were evaluated on <italic>Lactobacillus casei</italic> NBMCC-1013 [<xref ref-type="bibr" rid="B20">20</xref>]. Almost all these studies (except [<xref ref-type="bibr" rid="B28">28</xref>,<xref ref-type="bibr" rid="B29">29</xref>]) are based on biomass growth and/or lactic acid production.</p>
			<p>Also, it has been shown in the scientific literature that toxicity studies of the several organic solvents on different microorganisms have been contradictory [<xref ref-type="bibr" rid="B20">20</xref>], showing that the toxicity is highly related with the type and even the kind of strain of the microorganism. On the other hand, most of the studies have been focused on analyzing the lactic acid production and/or cell growth but rarely glucose consumption has been taken into account.</p>
			<p>In this work, the molecular toxicity of three diluents (dodecane, dodecanol, and oleyl alcohol) and three carriers (trioctylamine, tri-iso-octylamine and Aliquat 336), with high potential to be used in lactic acid removal by perstraction or reactive liquid extraction was measured on the bacteria <italic>Lactobacillus casei</italic> ATCC 393. Also, the molecular toxicity of mixtures trioctylamine/n-dodecane and tri-iso-octylamine/n-dodecane were evaluated at three different volumetric ratios. The toxic effects were analyzed by measuring biomass growth, lactic acid production, and glucose consumption.</p>
		</sec>
		<sec sec-type="materials|methods">
			<title>2. Materials and methods</title>
			<p>Molecular toxicity of n-dodecane (Merck, assay 99 %), 1-dodecanol (Merck, assay 98 %) and oleyl alcohol (Merck, assay 85 %) as diluents and trioctylamine (TOA, Merck, assay 93 %), tri-iso-octylamine (TiOA, Merck, assay 95 %) and Aliquat 336 (Sigma-Aldrich) as extractants were evaluated separately on cell growth of the bacteria <italic>Lactobacillus casei</italic> ATCC 393 (Microbiologics) using MRS (Sharlau) culture media.</p>
			<p>The experimental design for toxicity was first with pure carriers and solvents. For the solvent with the lowest toxicity, the experiments were carried out with amine (TOA, TiOA) concentrations at three levels in the range of concentration reported in the literature for liquid membrane or liquid extraction applications [<xref ref-type="bibr" rid="B6">6</xref>,<xref ref-type="bibr" rid="B26">26</xref>]. Aliquat 336 was not tested in mixtures with solvent due to its high toxicity. All experiments were carried out with duplicates.</p>
			<p>In every single test for each pure substance, 100 mL of culture media was prepared and added into a 250 mL glass flask. Afterward, the organic compounds were added in order to achieve a volume ratio of 1:10 (organic compound:culture media). The six flasks, one for every organic compound (n-dodecane, dodecanol, oleyl alcohol, TOA, TiOA, Aliquat), were shacked using a magnetic stirrer (Velp Scientifica) at 120 rpm and constant temperature of 310 K in an incubator (Binder RI 115, ± 0.3 K) for 72 h (contact stage). Then, the agitation was stopped, each flask was transferred to separation funnels and kept in an oven at 310 K during 72 h for phase splitting (aqueous from the organic phase). Subsequently, the phases were separated.</p>
			<p>Volumes of 7.5, 15, 22.5 and 30 mL of each aqueous phase, previously saturated with an organic phase (described above), were taken and mixed with fresh culture media to reach a total volume of 30 ml using Falcon centrifuge tubes of 50 mL. These volumes correspond to proportions of 25 %, 50 %, 75 % and 100 vol%. Then, each culture media was inoculated at 5 vol% with <italic>Lactobacillus casei</italic> ATCC 393 from an inoculum of 12 h. One control (fermentation without toxic agents) was prepared using fresh culture media. At the beginning of the fermentation (previous to inoculum step, 0 h) and at the end (24 h) one sample was extracted from each Falcon tube (6 (mixtures) x 4 (levels) x 2 (duplicates) = 48 tubes) in order to quantify the glucose consumption, lactic acid and biomass production (in percentage referred to control fermentation). Bacterial growth was measured by optical density (OD at the maximum wavelength, 540 nm) using a spectrophotometer (V1200, Mapada Instruments) and by dry cell weight method [<xref ref-type="bibr" rid="B30">30</xref>]. Lactic acid production and glucose consumption were measured by HPLC (ELITE LaChrom) using ORH-801 column (Chrom Tech) with a RI detector at 318.15 K using as a mobile phase a solution of 0.01 N H<sub>2</sub>SO<sub>4</sub> (Merck, assay 95-97 %) prepared with type 1 water (Barnstead™ Nanopure™). Every single Falcon tube was kept in an oven at 310 K for 24 h.</p>
			<p>Trioctylamine and tri-iso-octylamine were mixed at concentrations of 10, 20 and 30 vol% with n-dodecane (0 % of amine corresponds to previous experiments with pure dodecane) and its molecular toxicity level were tested following the aforementioned procedure using 30 mL of the aqueous phase (from the phase splitting) for the fermentation step. These concentration of the amine are typical for liquid membranes and liquid extraction [<xref ref-type="bibr" rid="B6">6</xref>,<xref ref-type="bibr" rid="B13">13</xref>,<xref ref-type="bibr" rid="B26">26</xref>]. As it is shown below, Oleyl alcohol and dodecanol were excluded due to their high toxicity compared to dodecane.</p>
		</sec>
		<sec sec-type="results|discussion">
			<title>3. Results and discussion</title>
			<p>Based on the classification of J. Marták <italic>et al</italic>. [<xref ref-type="bibr" rid="B29">29</xref>], organic solvents can be divided into three groups according to their toxicity level on microorganisms. Non-toxic, when the production rate is beyond 75 %, medium toxicity when the production rate is between the 25 % and 75 %, and toxic when the production rate is less than 25 % as compared with a control fermentation.</p>
			<sec>
				<title><italic>3.1. Molecular toxicity for pure solvents</italic></title>
				<p>
					<xref ref-type="fig" rid="f1">Figs. 1</xref>-<xref ref-type="fig" rid="f3">3</xref> show the relative lactic acid (LA) production, cell growth and glucose consumption of a fermentation broth composed of a mixture of fresh culture media and saturated culture media with the specific solvent at proportions of 25, 50, 75 and 100 vol%, (referred to the saturated culture media). <xref ref-type="fig" rid="f1">Figs. 1</xref>-<xref ref-type="fig" rid="f3">3</xref> are based on a culture media that were not in contact with the studied organic compounds (control fermentation) and for which the LA production, cell growth, and glucose consumptions were also measured. Taking into account the Marták criteria [<xref ref-type="bibr" rid="B29">29</xref>], dodecane was non-toxic for the four tested proportions. Cell growth and LA production were still 16% lower than the control fermentation at the four proportions, while glucose consumption was still 6% higher. For dodecane molecular toxicity test, the glucose concentration in the culture media increases after the contact stage due to the transport of water and some nutrients from the culture media to the organic phase. Thus, the glucose concentration of the saturated culture media was between 1.4% and 5.3 % (SD = 1.5 - 7.6%), higher than the control fermentation, and in consequence, the glucose consumption was promoted achieving values of glucose consumption slightly above the 100 %. Taking into account a higher glucose consumption is expected an increase in biomass and LA production. However, they were till 10% lower but within the standard deviation (maximum SD = 11.2%). The toxicity of dodecane on the bacteria was low enough that it does not have an important effect on the measured fermentation variables.</p>
				<p>
					<fig id="f1">
						<label>Figure 1</label>
						<caption>
							<title>Relative lactic acid production for each pure substance at four proportions of the saturated culture media.</title>
						</caption>
						<graphic xlink:href="0012-7353-dyna-85-207-360-gf1.png"/>
						<attrib><bold>Source:</bold> The authors</attrib>
					</fig>
				</p>
				<p>
					<fig id="f2">
						<label>Figure 2</label>
						<caption>
							<title>Relative cell growth by dry weight for each pure substance at four proportions of the saturated culture media.</title>
						</caption>
						<graphic xlink:href="0012-7353-dyna-85-207-360-gf2.png"/>
						<attrib><bold>Source:</bold> The authors</attrib>
					</fig>
				</p>
				<p>
					<fig id="f3">
						<label>Figure 3</label>
						<caption>
							<title>Relative glucose consumption for each pure substance at four proportions of the saturated culture media.</title>
						</caption>
						<graphic xlink:href="0012-7353-dyna-85-207-360-gf3.png"/>
						<attrib><bold>Source:</bold> The authors</attrib>
					</fig>
				</p>
				<p>Oleyl alcohol was non-toxic for volumetric proportions from 25 to 75 % considering LA production, cell growth, and glucose consumption (with a minimum and maximum standard deviation of ±0.9 and ±19.6). However, it can be observed that for cell growth (<xref ref-type="fig" rid="f2">Fig. 2</xref>) at proportions from 25 to 75 %, alcohol can be classified as medium toxic if the standard deviations are taking into account. Oleyl alcohol was medium toxic for a proportion of 100 % based on LA production, cell growth, and glucose consumption (with a minimum and maximum standard deviation of ±5.6 and ±18). The glucose consumption (<xref ref-type="fig" rid="f3">Fig. 3</xref>) was reduced by 20 % for 25, 50 and 75 % proportions and it was reduced by 30 % for a proportion of 100 %. On the other hand, both cell growth and LA production decrease around 20 % for proportions of 25, 50 and 75 % and around 30 % for a proportion of 100 %. These results seem to indicate that the bacteria use glucose equitably to produce LA and biomass when oleyl alcohol is present.</p>
				<p>Dodecanol has a medium toxicity for a proportion of 25 %, and it was toxic for the other proportions based on LA production and cell growth (<xref ref-type="fig" rid="f1">Fig. 1</xref>). However, glucose consumption was reduced around 40 % for a proportion of 25 % and around 60 % for proportions of 50, 75 % and 100 %. Also, cell growth rate was reduced by 60 % for a proportion of 25 % and around 90 % for proportions of 50, 75 % and 100 %. LA production was reduced around 50 % for a proportion of 25 % and around 80 % for the other proportions. The aforementioned results show that the bacteria consumes more glucose to survive than the biomass and LA produced. It uses this glucose for maintenance and this behavior is more intense at proportions above 50 % where there are a lower cell growth and LA production as compared to the glucose consumption. </p>
				<p>Aliquat 336 (a quaternary ammonium salt mixed with tertiary amines C8-C10-alkyl, octanol, and decanol) was toxic for all tested proportions, taking into account both LA produced and cell growth. LA produced was reduced by 95 % as compared with control fermentation. The consumed glucose was reduced around 95 % for volumetric proportions of 25, 75 and 100 %, but it was reduced by 86 % for a proportion of 50 %. The cell growth was reduced around 95 % for proportions of 25 and 100 % and it was reduced by 88 % for a proportion of 50 %. The aforementioned results show that the bacteria use the consumed glucose to produce biomass but reduce its LA production to survive and for maintenance. For a proportion of 75 % the cell growth was reduced by 82 %. At this point, the bacteria produced an amount of LA in accordance with the consumed glucose but the relative fraction of biomass produced was higher than the consumed glucose. Aliquat 336 was the most toxic amine among tested extractants. Aliquat 336 contains trioctylmethylammonium chloride (TOMAC) that has a chloride ion in its structure and can interact with some substances from the MRS, such as sodium acetate and triammonium citrate to produce sodium chloride and ammonium chloride. Ammonium chloride is soluble in water and increases the medium acidity, whereas low pH can inhibit the lactic acid bacteria [<xref ref-type="bibr" rid="B11">11</xref>,<xref ref-type="bibr" rid="B16">16</xref>,<xref ref-type="bibr" rid="B31">31</xref>].</p>
				<p>Trioctylamine (TOA) is toxic for the four volumetric proportions tested. Based on the cell growth, it is medium toxicity for a proportion of 25 % in terms of LA production and it is toxic for the other proportions. However, this value of medium toxicity could be read as toxic considering the standard deviation. The consumed glucose is used to equitably produce LA and biomass for proportions of 75 and 100 %, and as well for a proportion of 50 % if the standard deviations of glucose consumption and cell growth are taking into account. For a proportion of 25 %, the glucose consumption and LA production were reduced by 75 % but cell growth was reduced by 85 %, showing that the bacteria reduces its biomass production for maintenance.</p>
				<p>Tri-iso-octylamine (TiOA) was the only extractant that exhibited a medium toxicity. It was medium toxic for a proportion of 25 %, the other proportions and the other amines were toxic based on both, cell growth and LA production. TOA and TiOA are tertiary amines with the same structural formula thus it can be expected the same toxicity level. However, TiOA was less toxic than TOA. The <italic>iso</italic> structure into the alkyl group for TiOA can produce steric effects that probably reduces its toxic effects.</p>
				<p>Although it is known that toxicity of organic solvents depend on the type of microorganism or even of its strain [<xref ref-type="bibr" rid="B10">10</xref>,<xref ref-type="bibr" rid="B29">29</xref>,<xref ref-type="bibr" rid="B34">34</xref>], generally the toxicity is related to the solvent polarity (related to log P<sub>ow</sub> values - <xref ref-type="table" rid="t1">Table 1</xref>) [<xref ref-type="bibr" rid="B1">1</xref>,<xref ref-type="bibr" rid="B19">19</xref>,<xref ref-type="bibr" rid="B24">24</xref>], and its water solubility [<xref ref-type="bibr" rid="B10">10</xref>,<xref ref-type="bibr" rid="B25">25</xref>]. Therefore, it is expected that dodecanol and oleyl alcohol, which are polar, were more toxic than dodecane (non-polar). The toxicity with the alkane is similar to other studies where alkanes were non-toxic or low toxic on bacteria [<xref ref-type="bibr" rid="B29">29</xref>,<xref ref-type="bibr" rid="B35">35</xref>]. For alcohols, it is known that its toxicity decreases as its long-chain increases [<xref ref-type="bibr" rid="B1">1</xref>,<xref ref-type="bibr" rid="B29">29</xref>,<xref ref-type="bibr" rid="B35">35</xref>,<xref ref-type="bibr" rid="B36">36</xref>]. Also, this study shows that oleyl alcohol (C18) is less toxic than dodecanol (C12) on the bacteria <italic>Lactobacillus casei</italic> ATCC 393 (<xref ref-type="fig" rid="f2">Fig. 2</xref>).</p>
				<p>
					<table-wrap id="t1">
						<label>Table 1</label>
						<caption>
							<title>Main physical properties of the tested solvents related with its toxicity on microorganisms.</title>
						</caption>
						<graphic xlink:href="0012-7353-dyna-85-207-360-gt1.png"/>
						<table-wrap-foot>
							<fn id="TFN1">
								<p>Physical properties were calculated with ProPed-ICAS 14 software (CAPEC-DTU) using Marrero and Gani, Constantinou and Gani methods [<xref ref-type="bibr" rid="B32">32</xref>,<xref ref-type="bibr" rid="B33">33</xref>]. Water solubility was taken from MSDS. <sup>a</sup>Physical property at 293.15 K. <sup>b</sup>Physical property calculated for TOMAC using connectivity index neglecting ionic bond.</p>
							</fn>
							<fn id="TFN2">
								<p><bold>Source:</bold> The authors</p>
							</fn>
						</table-wrap-foot>
					</table-wrap>
				</p>
				<p>The logarithm of P<sub>ow</sub> (<xref ref-type="table" rid="t1">Table 1</xref>) is a common parameter to study toxic effects on microorganisms [<xref ref-type="bibr" rid="B24">24</xref>,<xref ref-type="bibr" rid="B37">37</xref>]. A Log P<sub>ow</sub> higher than 4, apparently does not have any effect on the biocatalytic activity of the cell [<xref ref-type="bibr" rid="B37">37</xref>]. However, a type of <italic>Lactobacillus Delbruekii</italic> is sensitive to organic solvents with Log P<sub>ow</sub> between 1 to 4 [<xref ref-type="bibr" rid="B24">24</xref>]. Taking into account Log P<sub>ow</sub> as a parameter of toxicity [<xref ref-type="bibr" rid="B24">24</xref>,<xref ref-type="bibr" rid="B37">37</xref>], the tested solvents can be considered to be low toxic, except dodecanol that it can be considered as non-toxic due to its Log P<sub>ow</sub> value, nevertheless, another scientific literature have shown that Log P<sub>ow</sub> is an unreliable parameter [<xref ref-type="bibr" rid="B1">1</xref>] to infer the toxicity level. However, other parameters as solubility and surface tension can affect the microbial growth (biomass and LA production, and glucose consumption).</p>
				<p>Surface tension and water solubility have also been used to predict the toxic effect of the solvent on the microorganism. A high surface tension involves a rapid loss of cellular activity [<xref ref-type="bibr" rid="B19">19</xref>,<xref ref-type="bibr" rid="B37">37</xref>] where the cell membrane fluidity increases [<xref ref-type="bibr" rid="B19">19</xref>]. Also, the lower the solvent solubility in water is, the lower the probability of contact between the solvent and the microorganism will be. Thus, microorganisms will be less affected for the solvent presence into the culture media. For these reasons oleyl alcohol is less toxic than dodecanol (water solubility in <xref ref-type="table" rid="t1">Table 1</xref>) in spite of having a similar surface tension. And dodecane has a low toxicity because it has a lower surface tension and lower water solubility than dodecanol and Oleyl alcohol.</p>
				<p>In extractants, the higher the surface tension is the higher the toxicity on the bacteria will be, resulting Aliquat 336 with the highest toxicity in spite of being the extractant with the lowest water solubility. The lower toxicity of TiOA as compared with TOA is due to TOA has a higher surface tension and in consequence, it disturbs the cell membrane function as a barrier, as a matrix for enzymes and as energy transducer [<xref ref-type="bibr" rid="B23">23</xref>].</p>
			</sec>
			<sec>
				<title><italic>3.2. Molecular toxicity of selected mixtures</italic></title>
				<p>
					<xref ref-type="fig" rid="f4">Figs. 4</xref>-<xref ref-type="fig" rid="f6">6</xref> shows lactic acid production, cell growth and glucose consumption (respectively) for the culture media after contact with mixes of TiOA or TOA (less toxic amines) in dodecane (less toxic diluent) at volumetric proportions of 10, 20 and 30 % of the respective tertiary amine in dodecane.</p>
				<p>
					<fig id="f4">
						<label>Figure 4</label>
						<caption>
							<title>Lactic acid production for TiOA/dodecane and TOA/dodecane mixtures at three proportions of the tertiary amine.</title>
						</caption>
						<graphic xlink:href="0012-7353-dyna-85-207-360-gf4.png"/>
						<attrib><bold>Source:</bold> The authors</attrib>
					</fig>
				</p>
				<p>
					<fig id="f5">
						<label>Figure 5</label>
						<caption>
							<title>Cell growth by dry weight for TiOA/dodecane and TOA/dodecane mixtures at three proportions of the tertiary amine.</title>
						</caption>
						<graphic xlink:href="0012-7353-dyna-85-207-360-gf5.png"/>
						<attrib><bold>Source:</bold> The authors</attrib>
					</fig>
				</p>
				<p>
					<fig id="f6">
						<label>Figure 6</label>
						<caption>
							<title>Glucose consumption for TiOA/dodecane and TOA/dodecane mixtures at three proportions of the tertiary amine.</title>
						</caption>
						<graphic xlink:href="0012-7353-dyna-85-207-360-gf6.png"/>
						<attrib><bold>Source:</bold> The authors</attrib>
					</fig>
				</p>
				<p>TiOA mixed in n-dodecane was non-toxic at the three volumetric proportions for both, LA production and cell growth. For cell growth, the toxicity effect on the bacteria rises as the TiOA concentration increases, being non-toxic for volumetric proportions of 10 and 20 % and medium toxic at 30 %. There is a LA production according to the glucose consumption for three proportions of TiOA. However, as TiOA concentration rises, the cell growth decreases, perhaps in order to survive due to a high energy consumption of the bacteria trying to tolerate the organic solvent. These microorganisms have developed several mechanisms to increase its tolerance for organics solvents, one of them involves the action of efflux pumps to expel the organic solvent cumulated into the membrane and another one involves to change the membrane rigidity in order to do it less permeable to the organic solvents [<xref ref-type="bibr" rid="B21">21</xref>]. Both mechanisms require an additional energy consumption.</p>
				<p>TOA was non-toxic at a volumetric proportion of 10 % for LA production and it was medium toxic for both cell growth and glucose consumption. It was medium toxicity at 20 % of TOA and toxic at 30 %. It means that the higher the TOA concentration is the higher the toxicity effect on the bacteria will be. For both proportions 20 and 30 % of TOA, the consumed glucose was used, in higher proportion, to produce LA than biomass. LA production is proportional to the glucose consumed but the biomass production is reduced. This means that for every single cell the LA production is increased as compared to the control fermentation. The metabolic changes inside the cell do not clearly explain this behavior.</p>
			</sec>
		</sec>
		<sec sec-type="conclusions">
			<title>4. Conclusions</title>
			<p>Taking into account cell growth, lactic acid production and glucose consumption, molecular toxicity level follows this order: dodecanol &gt; oleyl alcohol &gt; dodecane and for the extractants, the order is: Aliquat 336 &gt; TOA &gt; TiOA. Comparing the extractans with the diluents, extractants have higher molecular toxicity level. However, these extractants require to be mixed with a non-toxic diluent that ideally has a small effect on its extraction capacity.</p>
			<p>Log P<sub>ow</sub> is not a convenient property to evaluate the toxicity of the tested solvents. There is not an apparent relation between this parameter and the toxicity of the solvent on the bacteria.</p>
			<p>Surface tension and water solubility of the solvents have a considerable influence on the toxicity on the microorganisms. Solvents with a high surface tension or water solubility are more toxic for the bacteria. It means, when a solvent is expected to be toxic for the microorganism, it is convenient to use an organic solvent with a low water solubility.</p>
			<p>Tertiary amines, (TiOA and TOA) mixed in dodecane, although were medium toxic and toxic respectively, inhibited cell growth and promoted the LA production (at proportions of 20 and 30 %). Conversely, TiOA at low concentration (10 %) was non-toxic and promoted cell growth instead of LA production.</p>
			<p>Both TiOA/dodecane and TOA/dodecane at a proportion of 10 % have potential to be used in perstraction processes due to its low molecular toxicity level, where the lactic acid can be removed externally to the bioreactor from a fermentation broth free of biomass.</p>
		</sec>
	</body>
	<back>
		<ack>
			<title>Acknowledgments</title>
			<p>The authors gratefully acknowledge the experimental assistance of Eng. Verónica Gomez. The financial support of Colciencias under calls 617, 645 and 647, and the financial support of National University of Colombia under projects 28046 and 31011 are kindly acknowledged.</p>
		</ack>
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			<fn fn-type="other" id="fn1">
				<label>How to cite:</label>
				<p> Pérez, A.D., Rodríguez-Barona, S. and Fontalvo, J., Molecular toxicity of potential liquid membranes for lactic acid removal from fermentation broths using Lactobacillus casei ATCC 393. DYNA, 85(207), pp. 360-366, Octubre - Diciembre, 2018.</p>
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			<fn fn-type="other" id="fn2">
				<label>A.D. Pérez,</label>
				<p> is a PhD. student, MSc. and BSc. in Chemical Engineering all of them from the Universidad Nacional de Colombia, campus Manizales, Colombia. He was the technical laboratory coordinator in the laboratory of process intensification and hybrid systems (2014-2017). He was teacher of kinetic and catalysis and teaching assistant in heat and transfer processes, both at Universidad Nacional de Colombia, campus Manizales, Colombia, 2013 and 2014, respectively. He is a member of the research group of application of new technologies since 2011. ORCID: 0000-0001-7896-0130</p>
			</fn>
			<fn fn-type="other" id="fn3">
				<label>S. Rodríguez-Barona,</label>
				<p> is a PhD. and an associate professor of the Chemical Engineering Department at the Universidad Nacional de Colombia, campus Manizales, Colombia. She is member of the research group of research group on lactic acid bacteria and their industrial biotechnological applications. Her research areas are probiotic bacteria, nutraceutical components, functional food and new products. ORCID: 0000-0002-2290-2238</p>
			</fn>
			<fn fn-type="other" id="fn4">
				<label>J. Fontalvo,</label>
				<p> is a PhD. and an associate professor of the Chemical Engineering Department at the Universidad Nacional de Colombia, campus Manizales, Colombia. He is the head of the research group of application of new technologies and the laboratory of process intensification and hybrid systems. His research has been focused on process intensification using membrane technology for reactive and separation systems. Some examples are hybrid distillation and pervaporation systems, hybrid reactors using membrane technology for production of esters, biofuels and some specialized compounds produced by fermentation. He is interested on new concepts for process design and integration. ORCID: 0000-0002-7868-8736</p>
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