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 <!DOCTYPE article PUBLIC "-//NLM//DTD JATS (Z39.96) Journal Publishing DTD v1.0 20120330//EN" "http://jats.nlm.nih.gov/publishing/1.0/JATS-journalpublishing1.dtd"> <article xmlns:mml="http://www.w3.org/1998/Math/MathML" xmlns:xlink="http://www.w3.org/1999/xlink" xmlns:xsi="http://www.w3.org/2001/XMLSchema-instance" article-type="research-article" dtd-version="1.0" xml:lang="en">
  <front>
    <journal-meta>
      <journal-id journal-id-type="publisher-id">JBBS</journal-id>
      <journal-title-group>
        <journal-title>Journal of Biotechnology and Biomedical Science</journal-title>
      </journal-title-group>
      <issn pub-type="epub">2576-6694</issn>
      <publisher>
        <publisher-name>Open Access Pub</publisher-name>
        <publisher-loc>United States</publisher-loc>
      </publisher>
    </journal-meta>
    <article-meta>
      <article-id pub-id-type="publisher-id">JBBS-20-3419</article-id>
      <article-id pub-id-type="doi">10.14302/issn.2576-6694.jbbs-20-3419</article-id>
      <article-categories>
        <subj-group>
          <subject>research-article</subject>
        </subj-group>
      </article-categories>
      <title-group>
        <article-title>Biosorption of Lead Using the Bacterial Strain, <italic>Bacillus subtilis</italic> (MTCC 2423) </article-title>
        <alt-title alt-title-type="running-head">biosorption of lead using bacteria</alt-title>
      </title-group>
      <contrib-group>
        <contrib contrib-type="author">
          <name>
            <surname>Shivani</surname>
            <given-names>Gupta</given-names>
          </name>
          <xref ref-type="aff" rid="idm1842544508">1</xref>
        </contrib>
        <contrib contrib-type="author">
          <name>
            <surname>A.</surname>
            <given-names>Surendran</given-names>
          </name>
          <xref ref-type="aff" rid="idm1842559532">2</xref>
        </contrib>
        <contrib contrib-type="author">
          <name>
            <surname>A.</surname>
            <given-names>JosephThatheyus</given-names>
          </name>
          <xref ref-type="aff" rid="idm1842559532">2</xref>
          <xref ref-type="aff" rid="idm1842561044">*</xref>
        </contrib>
      </contrib-group>
      <aff id="idm1842544508">
        <label>1</label>
        <addr-line>PG Department of Microbiology, The American College, Madurai, Tamil Nadu, India.</addr-line>
      </aff>
      <aff id="idm1842559532">
        <label>2</label>
        <addr-line>PG &amp; Research Department of Zoology, The American College, Madurai, Tamil Nadu, India.</addr-line>
      </aff>
      <aff id="idm1842561044">
        <label>*</label>
        <addr-line>Corresponding author</addr-line>
      </aff>
      <contrib-group>
        <contrib contrib-type="editor">
          <name>
            <surname>Yitong</surname>
            <given-names>Li</given-names>
          </name>
          <xref ref-type="aff" rid="idm1842394444">1</xref>
        </contrib>
      </contrib-group>
      <aff id="idm1842394444">
        <label>1</label>
        <addr-line>Department of ONCOLOGY </addr-line>
      </aff>
      <author-notes>
        <corresp>
    
    Thatheyus A.J, <addr-line>Associate Professor &amp; Head, PG &amp; Research Department of             Zoology, The American College, Madurai – 625 002, Tamil Nadu, India.</addr-line> E-mail: <email>ajt@americancollege.edu.in</email></corresp>
        <fn fn-type="conflict" id="idm1842197332">
          <p>The authors have declared that no competing interests exist.</p>
        </fn>
      </author-notes>
      <pub-date pub-type="epub" iso-8601-date="2020-07-13">
        <day>13</day>
        <month>07</month>
        <year>2020</year>
      </pub-date>
      <volume>2</volume>
      <issue>3</issue>
      <fpage>1</fpage>
      <lpage>14</lpage>
      <history>
        <date date-type="received">
          <day>07</day>
          <month>06</month>
          <year>2020</year>
        </date>
        <date date-type="accepted">
          <day>04</day>
          <month>07</month>
          <year>2020</year>
        </date>
        <date date-type="online">
          <day>13</day>
          <month>07</month>
          <year>2020</year>
        </date>
      </history>
      <permissions>
        <copyright-statement>© </copyright-statement>
        <copyright-year>2020</copyright-year>
        <copyright-holder>Shivani Gupta, et al.</copyright-holder>
        <license xlink:href="http://creativecommons.org/licenses/by/4.0/" xlink:type="simple">
          <license-p>This is an open-access article distributed under the terms of the Creative Commons Attribution License, which permits unrestricted use, distribution, and reproduction in any medium, provided the original author and source are credited.</license-p>
        </license>
      </permissions>
      <self-uri xlink:href="http://openaccesspub.org/jbbs/article/1401">This article is available from http://openaccesspub.org/jbbs/article/1401</self-uri>
      <abstract>
        <p>Lead removal efficiency of the bacterial strain, <italic>Bacillus subtilis</italic> (MTCC 2423) was tested with 200, 400, 600, 800 and 1000 ppm of lead in minimal broth for a period of ten days. Samples were tested for the level of lead every two days in each concentration and maximum removal was observed after six days of treatment. With the increase in lead concentration, both biomass and lead removal efficiency showed an increase. When tested with immobilized, dead and live cells, maximum removal was observed for immobilized cells. Among the sugars tested, monosaccharide sugars enhanced the biomass of <italic>B. subtilis</italic> during lead treatment and the results are discussed.</p>
      </abstract>
      <kwd-group>
        <kwd>Bacteria</kwd>
        <kwd>Heavy metals</kwd>
        <kwd>Bioremediation</kwd>
        <kwd>Industrial effluents</kwd>
        <kwd>Bacillus subtilis</kwd>
        <kwd>Isotherm.</kwd>
      </kwd-group>
      <counts>
        <fig-count count="6"/>
        <table-count count="4"/>
        <page-count count="14"/>
      </counts>
    </article-meta>
  </front>
  <body>
    <sec id="idm1842390628" sec-type="intro">
      <title>Introduction</title>
      <p>Heavy metals employed in industries are hazardous to human beings and other organisms. A sudden boost in the industrial activities has contributed quantitatively as well as qualitatively to the alarming increase in the discharge of metal pollutants into environmental sink, especially the aqueous      environment <xref ref-type="bibr" rid="ridm1850508348">1</xref><xref ref-type="bibr" rid="ridm1850571284">2</xref>. Heavy metals reaching aquatic systems undergo food chain concentration and cause disorders in higher trophic levels. This fact renders the removal of heavy metals from aqueous solutions indispensable <xref ref-type="bibr" rid="ridm1850579492">3</xref>. </p>
      <p>Lead is a well-known metal for its extensive industrial applications which is in the environment at the end of the industrial processes such as metal          finishing, metallurgical work, electroplating, chemical             manufacturing, mining, paint production and battery manufacturing. Overall, only a small amount of lead is present in the environment naturally. But, the level is elevated only because of human activities <xref ref-type="bibr" rid="ridm1850366116">4</xref><xref ref-type="bibr" rid="ridm1850369140">5</xref>. Most commonly children are exposed to lead through              lead-based paints, whereas, adults are exposed mainly through their nature of work. With relevance to the impact of heavy metals on human health, each heavy metal causes diverse effects as well as symptoms <xref ref-type="bibr" rid="ridm1850367988">6</xref>. Literature review suggested that lead has no significant role to play inside the human body. At the same time, intake of lead through external sources create a variety of surplus effects like elevation of blood pressure, damage of kidney and brain, infertility in men, learning disability and behavioral distraction in children and others within human body <xref ref-type="bibr" rid="ridm1850354372">7</xref><xref ref-type="bibr" rid="ridm1850358764">8</xref><xref ref-type="bibr" rid="ridm1850347972">9</xref>.</p>
      <p>Several traditional practices such as ion exchange, filtration, evaporation, solvent extraction, electrochemical treatment, reverse osmosis, chemical precipitation and chemical oxidation or reduction are used to eliminate the toxic heavy metals dissolved in the industrial effluents. All these above mentioned processes are either very much expensive or not that much effective in removal process, in particular when the metal concentration is in the range of 1-100 mg/l in the waste water. An additional drawback of the traditional methods is the fabrication of more amount of toxic chemical sludge and its consequent disposal or treatment being further luxurious and also not environmental friendly <xref ref-type="bibr" rid="ridm1850343796">10</xref><xref ref-type="bibr" rid="ridm1850329316">11</xref><xref ref-type="bibr" rid="ridm1850324132">12</xref>. Hence, it is incredibly important to identify an eco-friendly, economically cheap and appropriate strategy for the elimination of the heavy metals present in waste water.  </p>
      <p>After several scientific investigations, bioremediation or biosorption technique has been concluded as a natural process and also cost effective. It has several advantages such as low operating cost, minimum ratio of disposable sludge volume, high efficiency in detoxifying very dilute effluents, multiple heavy metals uptake at a time, cheaper production of biomass, treatment of large volumes of waste water and even <italic>in situ</italic> remediation. It is a complex method which depends on various elements such as metal  concentration, chemical nature of metal ion, pH, temperature, contact time and composition of cell wall of microorganisms <xref ref-type="bibr" rid="ridm1850322188">13</xref><xref ref-type="bibr" rid="ridm1850318516">14</xref><xref ref-type="bibr" rid="ridm1850332052">15</xref><xref ref-type="bibr" rid="ridm1850297804">16</xref>. Various studies were carried out by several researchers regarding the biosorption of heavy metals using bacteria, fungi, algae and             yeast <xref ref-type="bibr" rid="ridm1850296940">17</xref><xref ref-type="bibr" rid="ridm1850309036">18</xref>. Among the various tested microorganisms, bacteria are identified as most promising candidate for removal of heavy metals especially for low concentration of heavy metals in waste water. Bacteria are a major group of living organisms present in soil and water. They are considered as the appropriate candidate to employ as an adsorbent because of their tiny nature and precise surface area. In particular, the chemical compounds such as carbonyl, hydroxyl, sulfhydryl, carboxyl, sulfonate, thioether, amine, amide, imine, phosphonate, imidazole, and phosphodiester group, present in their cell wall are competent in passively sequestering metals. Biosorption of heavy metals are very much influenced by several factors including binding strength, number of available binding sites and accessibility of binding site <xref ref-type="bibr" rid="ridm1850306444">19</xref><xref ref-type="bibr" rid="ridm1850302412">20</xref><xref ref-type="bibr" rid="ridm1850283932">21</xref>.     </p>
      <p>Microorganisms present in the metal polluted environment naturally develop the resistance against the toxicity of existing heavy metals <xref ref-type="bibr" rid="ridm1850281340">22</xref>. <italic>Bacillus subtilis </italic>is aerobic, rod-shaped and spore forming bacterium which is most commonly present in soil. It is non-toxic and          non-pathogenic in nature. It is capable of producing enzymes like proteases and amylase and has wide range of industrial applications as well. In recent times, it is used as model agent in laboratory research due to its simple genetic nature <xref ref-type="bibr" rid="ridm1850277452">23</xref><xref ref-type="bibr" rid="ridm1850274644">24</xref><xref ref-type="bibr" rid="ridm1850288684">25</xref>. Even though, there are some studies relevant to biosorption of heavy metals including lead by different strains of <italic>B. subtilis </italic>in the literature, there is no report on <italic>B. subtilis </italic>MTCC 2423 strain with reference to removal of lead. Hence in the present study, an attempt has been made to study the biosorption potential of the bacterial strain, <italic>Bacillus subtilis</italic> (MTCC 2423) for lead. Experiments have also been designed to study the biosorption potential of immobilized and dead cells of <italic>B. subtilis</italic> for lead and a comparison was done with that of live cells. It has also been planned to study the influence of different sugars on the biomass of <italic>B. subtilis</italic> during lead treatment. The findings of this study could be handy for the removal of heavy metals by <italic>B. subtilis </italic>(MTCC 2423) in industrial applications.</p>
    </sec>
    <sec id="idm1842389044" sec-type="materials">
      <title>Materials and Methods</title>
      <p>Various concentrations of lead were prepared by dissolving lead acetate [(CH<sub>3</sub>COO)<sub>2</sub>Pb.3H<sub>2</sub>O] in sterile distilled water.</p>
      <sec id="idm1842377916">
        <title>Strain Procurement and Maintenance</title>
        <p>            The bacterial strain <italic>B. subtilis</italic> (Strain No. MTCC 2423; ATCC 21331) used in the present study was obtained from Microbial Type Culture Collection (MTCC), IMTECH, Chandigarh, India. </p>
      </sec>
      <sec id="idm1842377556">
        <title>Determination of Metal Inhibition</title>
        <p>The maximum concentration of lead allowing bacterial growth was determined in nutrient agar (peptic digest of animal tissue-0.5g, beef extract-0.15g, yeast extract-0.15g, sodium chloride-0.5g and agar-1.5g in 100 ml of distilled water) having 50, 100, 500, 1000, 2000, 3000 and 4000 ppm of lead. Growth was observed after incubating the plates for 24 hrs at 37°C. </p>
      </sec>
      <sec id="idm1842376692">
        <title>Sample Preparation</title>
        <p>The organism from the overnight culture maintained in nutrient broth (peptic digest of animal tissue-0.5g, beef extract-0.15g, yeast extract-0.15g and sodium chloride-0.5g in 100 ml of distilled water) was inoculated (10<sup>9</sup> cells) into minimalbroth (dipotassium hydrogen phosphate-0.7g, potassium dihydrogen phosphate-0.2g, glucose-0.1g, sodium citrate-0.05g and magnesium sulphate-0.1g in 100 ml of distilled water) containing different concentrations of lead (200, 400, 600, 800 and 1000 ppm). The culture flasks incubated on a shaker for intermittent mixing were maintained at room temperature. The samples from these flasks were taken after every two days up to ten days and were subjected to AAS analysis for determining the residual lead concentration.</p>
      </sec>
      <sec id="idm1842374892">
        <title>Estimation of Residual Lead Concentration</title>
        <p>From each concentration ten ml sample was taken and centrifuged at 2500 rpm for fifteen minutes.  The supernatant was taken in an eppendorf tube and subjected to Atomic Absorption Spectrophotometric (AAS) analysis (Model: MSA030351; Thermo Fisher Scientific Ltd., India) and the readings were recorded.</p>
      </sec>
      <sec id="idm1842375180">
        <title>Biomass Estimation</title>
        <p>After centrifugation pellet was collected and dried in a hot air oven at 80°C  for 3 hrs. The final dry weight was taken to calculate the biomass.</p>
      </sec>
      <sec id="idm1842374820">
        <title>Preparation of Different cell Types</title>
        <p>For obtaining immobilized cells, the seed culture of the bacterium was grown in nutrient broth and the cells were harvested by centrifugation at 8000 rpm for twenty minutes. The cells were washed and suspended in 0.1% NaCl. Then 3.5% of sodium alginate was added to the cell suspension and mixed thoroughly without forming any air bubble in the slurry. The slurry containing cells was extended as drops through a tube (2mm diameter) into 4% CaCl<sub>2</sub> solution. The drops formed into spherical beads of 2mm size. The gel beads were kept in 4% CaCl<sub>2</sub> solution, at 5°C for about an hour for complete gelation <xref ref-type="bibr" rid="ridm1850237340">26</xref>. Then the beads were washed with sterile distilled water and used for lead biosorption study. For obtaining dead cells, the bacterial culture   (24 hrs) in nutrient broth was autoclaved at 121°C for thirty minutes and used for the study. The third type of cells used for the study was live cells, obtained from overnight culture of <italic>B. subtilis</italic> in nutrient broth.</p>
        <p>For comparing the efficiency of biosorption of live, dead and immobilized cells, 100 ml minimal broth with 1000 ppm of lead in 250 ml Erlenmeyer flasks was used. These flasks were inoculated with these cell types individually (10<sup>9</sup> cells for live and dead cells and ten beads for immobilized cells as inoculum volume). Samples were taken from these flasks after every 30 minutes upto 150 mins. Samples were centrifuged at 2500 rpm for fifteen minutes and the clean supernatant was  used for AAS analysis (Model: MSA030351; Thermo Fisher Scientific Ltd., India). The readings represented the mean of residual concentration of lead in solution.</p>
      </sec>
      <sec id="idm1842375540">
        <title>Supplementation of Sugars</title>
        <p>By supplementing different carbon sources like dextrose, fructose, glucose, lactose and sucrose at 10% concentration in minimal broth having 1000 ppm lead and the inoculum (10<sup>9</sup>cells), the efficiency of the bacterial strain for the removal of lead was also determined. The flasks were incubated at 37°C on a shaker for six days and the samples were centrifuged at 2500 rpm for 15 mins. The pellets were dried in a hot air oven at 80°C for 3 hrs and the biomass was estimated. </p>
      </sec>
      <sec id="idm1842372876">
        <title>Statistical Analysis</title>
        <p> Two way analysis of variance (ANOVA) was carried out for the factors, residual lead concentration, percent removal of lead and biomass of <italic>B. subtilis</italic> for the two variables, lead concentration and treatment period. It was also performed for the factors, residual lead concentration and percent removal of lead for different cell types with the variables, treatment period and cell types, using Microsoft MS- Excel package (Version: 12.0.6219.1000).</p>
      </sec>
      <sec id="idm1842373236">
        <title>Calculation of Lead Uptake</title>
        <p>Lead uptake by the bacterium was calculated using the following mass balance equation <xref ref-type="bibr" rid="ridm1850347972">9</xref>:</p>
        <p>Q = [V (C<sub>i</sub>-C<sub>f</sub>)]/S            (eq. 1)</p>
        <p>Where, q = lead uptake (mg metal/g cell dry weight);                    V = volume of metal-bearing solution contacted with the bacterium (L); C<sub>i </sub>= initial concentration of metal in solution (mg/L); C<sub>f</sub>= final concentration of metal in solution (mg/L); S = dry weight of bacterial cells added (g).</p>
      </sec>
      <sec id="idm1842379500">
        <title>Biosorption Models</title>
        <p>Freundlich <xref ref-type="bibr" rid="ridm1850235252">27</xref> and Langmuir <xref ref-type="bibr" rid="ridm1850233812">28</xref> isotherm models were applied for interpreting the lead biosorption equilibrium. </p>
        <p>The classical Freundlich equation is given below:</p>
        <p>q = K<sub>f</sub>C<sub>e</sub><sup>1/n           </sup>(eq. 2)</p>
        <p>Where, q = heavy metal adsorbed on the bacterium (mg/g dry weight); C<sub>e </sub>= final concentration of metal (mg/L) in the solution; K<sub>f</sub>= an empirical constant that provides an indication of the adsorption capacity of biosorbent; n = an empirical constant that provides an indication of the intensity of adsorption.</p>
        <p>Equation <xref ref-type="bibr" rid="ridm1850571284">2</xref> can be linearized as follows:</p>
        <p>Log q = log K<sub>f</sub><sub> +</sub> (1/n) log C<sub>e</sub>             (eq. 3)</p>
        <p>The adsorption constants, K<sub>f</sub>and 1/n were determined by plotting log q as a function of log C<sub>e</sub>.</p>
        <p>The classical Langmuir equation is given below:</p>
        <p>q = (Q<sub>max</sub> b C<sub>e</sub>)/ (1+ b C<sub>e</sub>)          (eq.4)</p>
        <p>Where, q = heavy metal adsorbed on the bacterium (mg/g dry weight); C<sub>e </sub>= final concentration of metal (mg/L) in the solution; Q<sub>max</sub>= maximum possible amount of metallic ion adsorbed per unit weight of bacterial cells; b = equilibrium constant related to the affinity of the binding sites for the metals.</p>
        <p>Equation <xref ref-type="bibr" rid="ridm1850366116">4</xref> can be linearized as follows:</p>
        <p>1/q = (1/q<sub>max</sub>) + (1/q<sub>max</sub>b) (1/C<sub>e</sub>)      (eq.5)</p>
        <p>The adsorption constants (Q<sub>max</sub>and b) were obtained by plotting 1/q as a function of 1/C<sub>e</sub>.</p>
      </sec>
    </sec>
    <sec id="idm1842362316" sec-type="results">
      <title>Results</title>
      <p>The bacterial strain, <italic>B. subtilis</italic> was tested for the metal tolerance with a wide range of lead concentrations (50, 100, 500, 1000, 2000, 3000 and 4000 ppm). The results indicate that after 24 hrs of incubation, <italic>B. subtilis</italic> grew well upto 1000 ppm concentration of lead. Based on the metal tolerance level, <italic>B. subtilis</italic> was subjected to different              concentrations of lead (200, 400, 600, 800 and 1000 ppm) in minimal broth for 10 days for studying its metal removal efficiency.</p>
      <p>The residual concentrations of lead after treatment with <italic>B. subtilis </italic>were determined (<xref ref-type="table" rid="idm1849164100">Table 1</xref>). The values of residual concentrations of lead after treatment with <italic>B. subtilis</italic> seem to be fluctuating. The minimum value of residual concentration of lead is observed at 400 ppm after 6 days of treatment period and maximum at 800 ppm after 10 days of treatment. <xref ref-type="fig" rid="idm1849124604">Figure 1</xref> illustrates the percent removal of lead after treatment with <italic>B. subtilis</italic>. It indicates that for all the treatment periods, the highest percent removal was for 1000 ppm concentration of lead, with the exception of the second and eighth day of treatment period. </p>
      <table-wrap id="idm1849164100">
        <label>Table 1.</label>
        <caption>
          <title> Residual concentration of lead (ppm) after treatment with Bacillus subtilis</title>
        </caption>
        <table rules="all" frame="box">
          <tbody>
            <tr>
              <td>Treatment period</td>
              <td colspan="5">Lead concentration (ppm)</td>
            </tr>
            <tr>
              <td>(days)</td>
              <td>200</td>
              <td>400</td>
              <td>600</td>
              <td>800</td>
              <td>1000</td>
            </tr>
            <tr>
              <td>2</td>
              <td>1.559</td>
              <td>0.114</td>
              <td>0.061</td>
              <td>0.046</td>
              <td>0.137</td>
            </tr>
            <tr>
              <td>4</td>
              <td>0.190</td>
              <td>0.200</td>
              <td>0.524</td>
              <td>0.540</td>
              <td>0.265</td>
            </tr>
            <tr>
              <td>6</td>
              <td>0.244</td>
              <td>0.031</td>
              <td>0.361</td>
              <td>1.532</td>
              <td>0.078</td>
            </tr>
            <tr>
              <td>8</td>
              <td>0.730</td>
              <td>0.220</td>
              <td>0.808</td>
              <td>0.894</td>
              <td>0.833</td>
            </tr>
            <tr>
              <td>10</td>
              <td>0.967</td>
              <td>0.158</td>
              <td>0.486</td>
              <td>1.583</td>
              <td>0.428 </td>
            </tr>
          </tbody>
        </table>
      </table-wrap>
      <fig id="idm1849124604">
        <label>Figure 1.</label>
        <caption>
          <title> Percent removal of lead after treatment with Bacillus subtilis</title>
        </caption>
        <graphic xlink:href="images/image1.jpg" mime-subtype="jpg"/>
      </fig>
      <p>The residual concentrations of lead after treatment with <italic>B. subtilis</italic> of different preparations were determined (<xref ref-type="table" rid="idm1849137996">Table 2</xref>). For each treatment period, live cells showed the highest value for the residual concentration of lead followed by autoclaved cells and immobilized cells. The biomass (g/ml) of <italic>B. subtilis</italic> during lead treatment showed that for each day the highest biomass obtained is with 1000 ppm      concentration of lead with the maximum after 6days of treatment. It indicates that lead concentration and biomass are directly proportional with each other. Highest biomass is obtained  for all the lead concentrations on the sixth day with respect to the treatment period (<xref ref-type="fig" rid="idm1849087708">Figure 2</xref>). </p>
      <table-wrap id="idm1849137996">
        <label>Table 2.</label>
        <caption>
          <title> Residual concentration of lead (ppm) after treatment with Bacillus  subtilis of different preparations for 1000 ppm lead concentration</title>
        </caption>
        <table rules="all" frame="box">
          <tbody>
            <tr>
              <td>Treatment period</td>
              <td colspan="3">Cell types</td>
            </tr>
            <tr>
              <td>(minutes)</td>
              <td>Live</td>
              <td>Autoclaved</td>
              <td>Immobilized</td>
            </tr>
            <tr>
              <td>30</td>
              <td>44.621</td>
              <td>12.871</td>
              <td>0.374</td>
            </tr>
            <tr>
              <td>60</td>
              <td>51.911</td>
              <td>27.417</td>
              <td>14.616</td>
            </tr>
            <tr>
              <td>90</td>
              <td>40.494</td>
              <td>13.619</td>
              <td>8.718</td>
            </tr>
            <tr>
              <td>120</td>
              <td>20.989</td>
              <td>19.471</td>
              <td>12.852</td>
            </tr>
            <tr>
              <td>150</td>
              <td>28.100</td>
              <td>14.732</td>
              <td>11.959 </td>
            </tr>
          </tbody>
        </table>
      </table-wrap>
      <fig id="idm1849087708">
        <label>Figure 2.</label>
        <caption>
          <title> Biomass (g/ml) of  Bacillus subtilis during lead treatment</title>
        </caption>
        <graphic xlink:href="images/image2.jpg" mime-subtype="jpg"/>
      </fig>
      <p><xref ref-type="fig" rid="idm1849101748">Figure 3</xref> reveals the percent removal of lead after treatment with <italic>B. subtilis</italic> of different preparations. It infers that immobilized cells are highly efficient in the sorption of lead, while the activity of autoclaved cells is lesser and least for live cells, for all the cases of treatment period. The maximum removal of lead by immobilized cells is observed after 30 mins.</p>
      <fig id="idm1849101748">
        <label>Figure 3.</label>
        <caption>
          <title> Percent removal of lead after treatment with Bacillus subtilis of different preparations</title>
        </caption>
        <graphic xlink:href="images/image3.png" mime-subtype="png"/>
      </fig>
      <p>The influence of various sugars at 10% concentration on the biomass of <italic>B. subtilis</italic> during lead treatment is exhibited in <xref ref-type="fig" rid="idm1849054412">Figure 4</xref>. It shows that biomass is the highest in the case of dextrose, followed by glucose, fructose, sucrose and lactose. This trend indicates that increased biomass is due to the influence of monosaccharides (dextrose, glucose and fructose) while with disaccharides (sucrose and lactose)                  the biomass decreases.</p>
      <fig id="idm1849054412">
        <label>Figure 4.</label>
        <caption>
          <title> Influence of sugars on the biomass (g/ml) of Bacillus subtilis during lead treatment</title>
        </caption>
        <graphic xlink:href="images/image4.jpg" mime-subtype="jpg"/>
      </fig>
      <p>Two way analysis of variance for the factor, residual concentration of lead with the variables, treatment period and lead concentration indicated that the variations in residual concentration of lead due to treatment period and lead concentration were not statistically significant at 5% level. The variations in residual concentration of lead due to cell types were not significant at 5% level but significant due to treatment period. The variations in the biomass (g/ml) of <italic>B. subtilis </italic>due to lead concentration and treatment period were statistically significant at 5% level.</p>
      <p>The variation in percent removal of lead due to cell types was not statistically significant at 5% level but significant due to treatment period. The variation in percent removal of lead due to lead concentration was not statistically significant at 5% level but significant due to treatment period (<xref ref-type="table" rid="idm1849051604">Table 3</xref>).</p>
      <table-wrap id="idm1849051604">
        <label>Table 3.</label>
        <caption>
          <title> Results of two way analysis of variance (ANOVA) for the various factors during the bioremediation of lead by Bacillus subtilis</title>
        </caption>
        <table rules="all" frame="box">
          <tbody>
            <tr>
              <td>Factor</td>
              <td>Source of variation</td>
              <td>Calculated F value</td>
              <td>F table value at 5% level</td>
              <td>Level ofsignificance</td>
            </tr>
            <tr>
              <td>Residual concentration of lead</td>
              <td>lead concentration</td>
              <td>0.84</td>
              <td>3</td>
              <td>Not significant (P&gt;0.05)</td>
            </tr>
            <tr>
              <td/>
              <td>treatment period</td>
              <td>2.51</td>
              <td>3</td>
              <td>Not significant (P&gt;0.05)</td>
            </tr>
            <tr>
              <td>Residual concentration of lead</td>
              <td>cell types</td>
              <td>0.95</td>
              <td>3.83</td>
              <td>Not significant (P&gt;0.05)</td>
            </tr>
            <tr>
              <td/>
              <td>treatment period</td>
              <td>11.27</td>
              <td>4.45</td>
              <td>Significant(P&lt;0.05)</td>
            </tr>
            <tr>
              <td>Biomass(g/ml) of <italic>B. subtilis</italic></td>
              <td>lead concentration</td>
              <td>48.8</td>
              <td>3</td>
              <td>Significant(P&lt;0.05)</td>
            </tr>
            <tr>
              <td/>
              <td>treatment period</td>
              <td>8.46</td>
              <td>3</td>
              <td>Significant(P&lt;0.05)</td>
            </tr>
            <tr>
              <td>Percent removal of lead</td>
              <td>lead concentration</td>
              <td>0.66</td>
              <td>3</td>
              <td>Not significant (P&gt;0.05)</td>
            </tr>
            <tr>
              <td/>
              <td>treatment period</td>
              <td>5.09</td>
              <td>3</td>
              <td>Significant(P&lt;0.05)</td>
            </tr>
            <tr>
              <td>Percent removal of lead</td>
              <td>cell types</td>
              <td>0.95</td>
              <td>3.83</td>
              <td>Not significant (P&gt;0.05)</td>
            </tr>
            <tr>
              <td/>
              <td>treatment period</td>
              <td>11.27</td>
              <td>4.45</td>
              <td>Significant(P&lt;0.05)</td>
            </tr>
          </tbody>
        </table>
      </table-wrap>
      <p>The Freundlich adsorption isotherms for lead biosorption by <italic>B. subtilis</italic> after every two days of treatment period are given in <xref ref-type="fig" rid="idm1849006244">Figure 5</xref>. The Langmuir adsorption isotherms for lead biosorption by <italic>B. subtilis</italic> after every two days of treatment period are given in <xref ref-type="fig" rid="idm1849003220">Figure 6</xref>. In Freundlich isotherm models, R<sup>2</sup> was the maximum after two days of treatment and it showed a decline with the increase in treatment period.                Kf was the highest after eight days of treatment while 1/n was the maximum after four days of treatment. In the case of Langmuir models, R<sup>2</sup> and Qmax were the highest after two days of treatment while b was the maximum after eight days of treatment (<xref ref-type="table" rid="idm1849000844">Table 4</xref>).</p>
      <fig id="idm1849006244">
        <label>Figure 5.</label>
        <caption>
          <title> Freundlich isotherm for lead biosorption by Bacillus subtilis after different days of treatment</title>
        </caption>
        <graphic xlink:href="images/image5.jpg" mime-subtype="jpg"/>
      </fig>
      <fig id="idm1849003220">
        <label>Figure 6.</label>
        <caption>
          <title> Langmuir isotherm for lead biosorption by Bacillus subtilis after different days of treatment</title>
        </caption>
        <graphic xlink:href="images/image6.jpg" mime-subtype="jpg"/>
      </fig>
      <table-wrap id="idm1849000844">
        <label>Table 4.</label>
        <caption>
          <title> Isotherm constants for lead biosorption by Bacillus subtilis</title>
        </caption>
        <table rules="all" frame="box">
          <tbody>
            <tr>
              <td>Treatment Period (days)</td>
              <td colspan="3">Isotherm constants</td>
            </tr>
            <tr>
              <td>2</td>
              <td>Freundlich</td>
              <td>R<sup>2</sup></td>
              <td>0.673</td>
            </tr>
            <tr>
              <td/>
              <td/>
              <td>Kf</td>
              <td>17.78</td>
            </tr>
            <tr>
              <td/>
              <td/>
              <td>1/n</td>
              <td>-0.445</td>
            </tr>
            <tr>
              <td/>
              <td>Langmuir</td>
              <td>R<sup>2</sup></td>
              <td>0.588</td>
            </tr>
            <tr>
              <td/>
              <td/>
              <td>Qmax (mg/g)</td>
              <td>1000</td>
            </tr>
            <tr>
              <td/>
              <td/>
              <td>b (L/mg)</td>
              <td>-0.001</td>
            </tr>
            <tr>
              <td>4</td>
              <td>Freundlich</td>
              <td>R<sup>2</sup></td>
              <td>0.443</td>
            </tr>
            <tr>
              <td/>
              <td/>
              <td>Kf</td>
              <td>25.12</td>
            </tr>
            <tr>
              <td/>
              <td/>
              <td>1/n</td>
              <td>0.364</td>
            </tr>
            <tr>
              <td/>
              <td>Langmuir</td>
              <td>R<sup>2</sup></td>
              <td>0.510</td>
            </tr>
            <tr>
              <td/>
              <td/>
              <td>Qmax (mg/g)</td>
              <td>50</td>
            </tr>
            <tr>
              <td/>
              <td/>
              <td>b (L/mg)</td>
              <td>0.035</td>
            </tr>
            <tr>
              <td>6</td>
              <td>Freundlich</td>
              <td>R<sup>2</sup></td>
              <td>0.071</td>
            </tr>
            <tr>
              <td/>
              <td/>
              <td>Kf</td>
              <td>1.413</td>
            </tr>
            <tr>
              <td/>
              <td/>
              <td>1/n</td>
              <td>0.176</td>
            </tr>
            <tr>
              <td/>
              <td>Langmuir</td>
              <td>R<sup>2</sup></td>
              <td>0.001</td>
            </tr>
            <tr>
              <td/>
              <td/>
              <td>Qmax (mg/g)</td>
              <td>16.66</td>
            </tr>
            <tr>
              <td/>
              <td/>
              <td>b (L/mg)</td>
              <td>-3.450</td>
            </tr>
            <tr>
              <td>8</td>
              <td>Freundlich</td>
              <td>R<sup>2</sup></td>
              <td>0.076</td>
            </tr>
            <tr>
              <td/>
              <td/>
              <td>Kf</td>
              <td>133.4</td>
            </tr>
            <tr>
              <td/>
              <td/>
              <td>1/n</td>
              <td>0.287</td>
            </tr>
            <tr>
              <td/>
              <td>Langmuir</td>
              <td>R<sup>2</sup></td>
              <td>0.117</td>
            </tr>
            <tr>
              <td/>
              <td/>
              <td>Qmax (mg/g)</td>
              <td>161.29</td>
            </tr>
            <tr>
              <td/>
              <td/>
              <td>b (L/mg)</td>
              <td>0.044</td>
            </tr>
            <tr>
              <td>10</td>
              <td>Freundlich</td>
              <td>R<sup>2</sup></td>
              <td>0.009</td>
            </tr>
            <tr>
              <td/>
              <td/>
              <td>Kf</td>
              <td>5.623</td>
            </tr>
            <tr>
              <td/>
              <td/>
              <td>1/n</td>
              <td>-0.017</td>
            </tr>
            <tr>
              <td/>
              <td>Langmuir</td>
              <td>R<sup>2</sup></td>
              <td>0.009</td>
            </tr>
            <tr>
              <td/>
              <td/>
              <td>Qmax (mg/g)</td>
              <td>71.42</td>
            </tr>
            <tr>
              <td/>
              <td/>
              <td>b (L/mg)</td>
              <td>0.079 </td>
            </tr>
          </tbody>
        </table>
      </table-wrap>
    </sec>
    <sec id="idm1842205668" sec-type="discussion">
      <title>Discussion</title>
      <p>Even low levels of lead can cause permanent damage in organisms. The immediate measure to prevent lead poisoning is to avoid exposure to lead. Removal of the source of lead is critical to reducing lead levels. Biosorption is an alternative to traditional      physico-chemical means for removing toxic metals from ground waters and waste waters. Removal of lead from solution was studied using growing cells and washed cells of <italic>Bacillus cereus </italic><xref ref-type="bibr" rid="ridm1850245980">29</xref>. The ability of the strain, <italic>B. subtilis</italic> to remove lead from solution was investigated in the present study. <italic>B. subtilis</italic> was reported to be the best for biosorbing lead among copper, zinc, lead and                 cadmium <xref ref-type="bibr" rid="ridm1850242164">30</xref>. <italic>B. subtilis</italic>, as a Gram positive organism has high capacity towards the binding with heavy metals, when compared with Gram negative bacteria because of their different cell wall structures. Phosphate groups present in the teichoic acids and other associated acids present in the Gram positive cell walls are the key factors responsible for the uptake of heavy metals present in the environment. The most important thing in the uptake of heavy metals are carboxyl groups, the sources  which are the teichoic acids in connection with peptidoglycon layers present in                      cell wall <xref ref-type="bibr" rid="ridm1850215172">31</xref><xref ref-type="bibr" rid="ridm1850211140">32</xref><xref ref-type="bibr" rid="ridm1850207756">33</xref>.</p>
      <p>When different concentrations of lead were tested, the strain <italic>B. subtilis</italic> was able to resist upto 1000 ppm. When the walls of <italic>B. subtilis</italic> were tested for the uptake of eighteen different metals, lead was shown to be taken up in small amounts into the wall <xref ref-type="bibr" rid="ridm1850202788">34</xref>. Maximum percent removal of lead was observed at 1000 ppm and minimum at 100 ppm. It indicates that at higher concentrations of lead, the uptake by <italic>B.subtilis</italic>is efficient. Efficient uptake of lead by <italic>B. subtilis</italic> can be explained on the basis of presence of some metal binding moieties on the surface of <italic>B. subtilis</italic>.  The important role of negatively charged carboxyl groups in lead biosorption by acetone washed biomass of <italic>Saccharomyces </italic><italic>uvarum</italic> was demonstrated <xref ref-type="bibr" rid="ridm1850200772">35</xref>.</p>
      <p>With different concentrations of lead, the biomass (g/ml) of <italic>B.subtilis</italic> obtained was the highest at 1000 ppm. It shows that biomass is directly proportional to increase in lead concentration. However, after six days the biomass again showed a decline. It indicates the saturation of metal binding moieties of <italic>B.subtilis</italic>. Lead ions show more affinity to algal biomass and they bind through a combination of ion-exchange, chelation and reduction reactions, along with metallic lead precipitation on the cell wall <xref ref-type="bibr" rid="ridm1850197172">36</xref>. When different preparations (live, dead and immobilized cells) of                        <italic>B. subtilis</italic> were exposed to 1000 ppm concentration of lead, immobilized cells, showed the highest percent removal. The highest biosorption of lead among Cu, Cd and Pb with multiple fixed beads containing immobilized bacterial biomass was studied <xref ref-type="bibr" rid="ridm1850226044">37</xref>. Two immobilized marine algae <italic>Sargassum </italic><italic>fluitans</italic> and <italic>Ascophyllum nodosum</italic> were used for the uptake of Cd, Cu, Ni, Pb and Zn. Both algae showed highest uptake for Pb <xref ref-type="bibr" rid="ridm1850224964">38</xref>. In the present study, autoclaved (dead) cells showed a higher percentage of lead removal than normal cells. In contrast with live cells, dead cells have several merits such as the capacity to treat huge amount of wastewater with less concentration of metals, less operation time, accessible without any dangerous byproducts and the lack of constraints on enzymatic activities produced by metal adsorption <xref ref-type="bibr" rid="ridm1850219420">39</xref>. Along with that, the dead cells do not need a constant nutrients requirement and  are not influenced by toxic wastes. It can be redeveloped and reused for several cycles. Therefore, the application of dead microbial cells in this practice has added benefits in removal of heavy metals from waste water <xref ref-type="bibr" rid="ridm1850218772">40</xref>.   </p>
      <p>In the present study, supplementation of different sugars (Dextrose, fructose, glucose, lactose and sucrose) indicated that dextrose, fructose and glucose were efficiently utilized by <italic>B. subtilis</italic>, which enhanced the biomass. The biomass was higher in the case of monosaccharides (dextrose, glucose and fructose) than that of disaccharides (lactose and sucrose) which imply that due to simple configuration of monosaccharides they are easily taken up by <italic>B. subtilis</italic> than disaccharides. Effect of carbon sources on dye decolourization by <italic>Aspergillus</italic> sp. was studied and it was demonstrated that the fungus reduces colour of dye by 98% in the presence of glucose (monosaccharide) and 92% in presence of sucrose (disaccharide) <xref ref-type="bibr" rid="ridm1850178644">41</xref>. </p>
      <p>The biosorption isotherm curve denotes the equilibrium distribution of metal ions between the aqueous and solid phases. The equilibrium distribution is very essential in finding out the highest biosorption potential. Various isotherm models are used to portray this equilibrium distribution. Langmuir and Freundlich models are extensively used in equilibrium analysis to analyse the mechanism of sorption <xref ref-type="bibr" rid="ridm1850176844">42</xref><xref ref-type="bibr" rid="ridm1850171084">43</xref><xref ref-type="bibr" rid="ridm1850168492">44</xref><xref ref-type="bibr" rid="ridm1850163812">45</xref><bold>. </bold>The Langmuir model considers sorption by monolayer type and presumes that all sorbent surface active sites have the similar affinity towards heavy metal ions <xref ref-type="bibr" rid="ridm1850161940">46</xref>. The Freundlich isotherm is an experimental equation which assumes a various biosorption system with diverse active sites <xref ref-type="bibr" rid="ridm1850158988">47</xref>. In the present study, the Freundlich and Langmuir isotherm coefficients were R<sup>2</sup>= 0.673, K<sub>f</sub>= 17.78, 1/n= -0.4452, R<sup>2</sup>= 0.5884, Q<sub>max</sub>= 1000 and       b= -0.0014. Ray <italic>et al</italic>. (2005) studied the           bioaccumulation of Pb (II) by <italic>Bacillus cereus</italic> (14). The isotherm coefficients were R<sup>2</sup>= 0.988, K<sub>f</sub>= 13.487, 1/n= 0.47, R<sup>2</sup>= 0.941, Q<sub>max</sub>= 70.423 and b= 0.214. Hence, it can be concluded that uptake of lead increased with increased concentration of lead. Biomass is also observed to be influenced by increasing lead concentration. Immobilized cells are shown to be highly efficient in lead uptake. Monosaccharides are observed to be effective on the biomass (g/ml) of <italic>B.subtilis</italic>.</p>
    </sec>
    <sec id="idm1842193284" sec-type="conclusions">
      <title>Conclusion</title>
      <p>Bioremediation is the major reason for the disappearance of these heavy metals from contaminated sites. However, the process is influenced by various environmental conditions like pH and temperature. The studies so far carried out suggest that <italic>B. subtilis</italic> endowed with all this properties of bioremediation enabled the biosorption and bioaccumulation of lead. Hence <italic>B.subtilis</italic> can be employed as an efficient organism for the effective uptake of lead and other heavy metals. </p>
      <sec id="idm1842194724">
        <title>Acknowledgments</title>
        <p>The authors thank the authorities of the American College, Madurai for the facilities and Tamil Nadu State Council for Science and Technology (TNSCST) Chennai for the financial assistance.</p>
      </sec>
    </sec>
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