<?xml version="1.0" encoding="UTF-8"?><!DOCTYPE article  PUBLIC "-//NLM//DTD Journal Publishing DTD v3.0 20080202//EN" "http://dtd.nlm.nih.gov/publishing/3.0/journalpublishing3.dtd"><article xmlns:mml="http://www.w3.org/1998/Math/MathML" xmlns:xlink="http://www.w3.org/1999/xlink" dtd-version="3.0" xml:lang="en" article-type="research article"><front><journal-meta><journal-id journal-id-type="publisher-id">JWARP</journal-id><journal-title-group><journal-title>Journal of Water Resource and Protection</journal-title></journal-title-group><issn pub-type="epub">1945-3094</issn><publisher><publisher-name>Scientific Research Publishing</publisher-name></publisher></journal-meta><article-meta><article-id pub-id-type="doi">10.4236/jwarp.2011.36055</article-id><article-id pub-id-type="publisher-id">JWARP-5743</article-id><article-categories><subj-group subj-group-type="heading"><subject>Articles</subject></subj-group><subj-group subj-group-type="Discipline-v2"><subject>Earth&amp;Environmental Sciences</subject></subj-group></article-categories><title-group><article-title>
 
 
  Adsorption Application for Removal of Hazardous Chloroform from Aqueous Solution by Nanocomposites Rectorite/Chitosan Adsorbent
 
</article-title></title-group><contrib-group><contrib contrib-type="author" xlink:type="simple"><name name-style="western"><surname>hiqian</surname><given-names>Li</given-names></name></contrib><contrib contrib-type="author" xlink:type="simple"><name name-style="western"><surname>Peijiang</surname><given-names>Zhou</given-names></name><xref ref-type="corresp" rid="cor1"><sup>*</sup></xref></contrib><contrib contrib-type="author" xlink:type="simple"><name name-style="western"><surname>Ling</surname><given-names>Ding</given-names></name></contrib></contrib-group><author-notes><corresp id="cor1">* E-mail:<email>zhoupj@whu.edu.cn(PZ)</email>;</corresp></author-notes><pub-date pub-type="epub"><day>29</day><month>06</month><year>2011</year></pub-date><volume>03</volume><issue>06</issue><fpage>448</fpage><lpage>455</lpage><history><date date-type="received"><day>March</day>	<month>2,</month>	<year>2011</year></date><date date-type="rev-recd"><day>April</day>	<month>11,</month>	<year>2011</year>	</date><date date-type="accepted"><day>May</day>	<month>21,</month>	<year>2011</year></date></history><permissions><copyright-statement>&#169; Copyright  2014 by authors and Scientific Research Publishing Inc. </copyright-statement><copyright-year>2014</copyright-year><license><license-p>This work is licensed under the Creative Commons Attribution International License (CC BY). http://creativecommons.org/licenses/by/4.0/</license-p></license></permissions><abstract><p>
 
 
  A novel nanocomposite bioadsorbent rectorite/chitosan was prepared by controlling different mass ratios of chitosan to rectorite using the water phase intercalation technique. The structure of the bioadsorbent was characterized by Fourier transform infrared (FT-IR) spectroscopy, X-ray diffraction (XRD) and scanning electron microscopy (SEM), Transmission electron microscopy (TEM), respectively. The results showed that the chitosan had been inserted into the rectorite layer successfully. The adsorption properties of the nanocomposite adsorbent toward CHCl3 from aqueous solution were investigated. Adsorption results showed that both nanocomposite adsorbents with weight ratio of rectorite to chitosan of 3:1 and 5:1 exhibited higher adsorption capacities.
 
</p></abstract><kwd-group><kwd>Nanocomposite Bioadsorbent; CHCl3 from Aqueous Solution; Adsorption.</kwd></kwd-group></article-meta></front><body><sec id="s1"><title>1. Introduction</title><p>Chloroform (trichloromethane, CHCl<sub>3</sub>) has been observed in the environment over many years; in air [<xref ref-type="bibr" rid="scirp.5743-ref1">1</xref>], water [<xref ref-type="bibr" rid="scirp.5743-ref2">2</xref>] and soil pores [<xref ref-type="bibr" rid="scirp.5743-ref3">3</xref>]. It is also presented in treated potable water [4-6], indeed misinterpretation of the significance of this chloroform content led one government health authority to stop treating drinking water with disastrous consequences [<xref ref-type="bibr" rid="scirp.5743-ref7">7</xref>]. The sources of most of the environmental flux are poorly characterized and the purpose of this work is to draw together the current state of knowledge. In the course of this, the effects of the chloroform flux induced by human activity should be placed into the context of the overall ecotoxicological and human health effects arising from the total flux. Significant use has been made of the comprehensive prior assessments of Zok et al. [<xref ref-type="bibr" rid="scirp.5743-ref2">2</xref>] and an expanded version of this paper, containing details of all the determinations used, has been reported by Euro Chlor [<xref ref-type="bibr" rid="scirp.5743-ref8">8</xref>].</p><p>Owing to the adverse effects, a number of techniques such as biodegradable [<xref ref-type="bibr" rid="scirp.5743-ref9">9</xref>], Hphotocatalytic oxidation [<xref ref-type="bibr" rid="scirp.5743-ref10">10</xref>], reverse osmosis, Wet Air Oxidation, and electro-deposition have been used to remove the toxic chloroform from aquatic environment [<xref ref-type="bibr" rid="scirp.5743-ref11">11</xref>]. However, these methods are not widely used due to their high cost and low feasibility for small-scale industries [<xref ref-type="bibr" rid="scirp.5743-ref12">12</xref>]. In contrast, the adsorption technique is one of the preferred methods for removal of chloroform because of its efficiency and low cost. Therefore, searching for efficient and affordable adsorption materials to purify the wastewater containing chloroform is of great significance [<xref ref-type="bibr" rid="scirp.5743-ref13">13</xref>].</p><p>Chitosan is a high molecular weight polysaccharide composed mainly of b-(1,4)-linked 2-deoxy-2-aminodglucopyranose units and partially of b-(1,4)-linked 2-deoxy-2-acetamido-d-glucopyranose. It has the properties of biocompatibility, biodegradability and avirulence, etc. So chitosan has been used in many areas [14-16]. For example, due to its properties of high mechanical strength, hydrophilic character, good adhesion and non-toxicity, chitosan is usually applied as food additive, supporting material for chromatography and adsorbent polymer for chloroform removal [17-20], the cationic biopolymer chitosan can be intercalated in Ca<sup>2+</sup>-rectorite through cationic exchange and hydrogen bonding processes, the resulting nanocomposites showing interesting structural and functional properties. Polymer/clay nanocomposites are of great interest because they combine the structure of physical and chemical properties of both inorganic and organic materials. Compared to the pure polymers, these nanocomposites demonstrate excellent properties such as improved storage modulus [<xref ref-type="bibr" rid="scirp.5743-ref21">21</xref>], decreased thermal expansion coefficients [<xref ref-type="bibr" rid="scirp.5743-ref22">22</xref>], reduced gas permeability [<xref ref-type="bibr" rid="scirp.5743-ref23">23</xref>], and enhanced ionic conductivity [<xref ref-type="bibr" rid="scirp.5743-ref24">24</xref>].</p><p>Rectorite is a kind of layered silicate, the structure and characteristics are much similar to those of montmorillonite. It is referred as an interstratified clay mineral made of regular 1:1 stacking of dioctahedral mica-like layer (nonexpansible) and dioctahedral montmorillonite-like layer (expansible). The cations of Na<sup>+</sup>, K<sup>+</sup> and Ca<sup>2+</sup> that contained lie in the interlayer region between 2:1 mica-like layers and 2:1 smectite-like layers, while the exchangeable hydrated cations reside in the latter. The REC structure can also cleave easily between smectite-like interlayers, forming monolithic REC layers of 2 nm thick. The interlayer cations can be exchanged easily by either organic or inorganic cations, and therefore rectorite has a property of water swelling similar to that of montmorillonite, which makes it possible to prepare chitosan/rectorite nanocomposites by solution-mixing processing technique. Therefore, in this study an attempt has been made to intercalate chitosan into the interlayers of the silicate, meanwhile, exhibiting this technique to develop new organic-inorganic hybrid materials provided with properties that are inherent to both types of components is also the purpose of the study [<xref ref-type="bibr" rid="scirp.5743-ref25">25</xref>].</p><p>In this study, a new clay/ploymer nanocomposite biosorbent were prepared by chitosan intercalation rectorite. Their structures were characterized by XRD, SEM and FT-IR techniques. It has been investigated that nanocomposite biosorbent have been used to remove CHCl<sub>3 </sub>from aqueous solution. rectorite/chitosan (REC/CS) nanocomposite biosorbent with the molar ratio of REC to CS of 3:1 showed good adsorption ability for CHCl<sub>3 </sub>from aqueous solution [<xref ref-type="bibr" rid="scirp.5743-ref26">26</xref>].</p></sec><sec id="s2"><title>2. Experimental</title><sec id="s2_1"><title>2.1. Materials</title><p>Chitosan (CS) was obtained from Golden-shell Biochemical Co. Ltd., China (Zhejiang, China). Its degree of deacetylation and the apparent viscosity were determined as 92%, and its average molecular weight was 2.1 &#215; 10<sup>5</sup> (determined by GPC method) [<xref ref-type="bibr" rid="scirp.5743-ref27">27</xref>]. Rectorite (REC) refined from the clay minerals was provided by Hubei Mingliu Inc. Co. (Wuhan, China). All of the used chemical reagents in experiment were analytical grade, and solutions were prepared with ultrapure water. The stock solutions of CHCl<sub>3</sub> (1000 mg/L) were prepared from analytical grade CHCl<sub>3</sub> using ultrapure water and serially diluted to working solutions of varying initial concentrations for experimental purpose. 1 mol/l NaOH and HCl were used to adjust the pH of the solutions.</p></sec><sec id="s2_2"><title>2.2. Preparation of CS-REC Nanocomposites Biosorbent</title><p>The 2% (w/v) solutions were prepared by dissolving an exact amount of CS in 1% (v/v) acetic acid and stirring for about 4 h [<xref ref-type="bibr" rid="scirp.5743-ref14">14</xref>]. The resulting solution was added slowly into the pretreated REC suspensions under stirring at 50˚C to obtain nanocomposites with initial REC/CS molar ratios of 1:1, 2:1, 3:1, 4:1, 5:1, The resulting mixture was agitated for 1 day, and then precipitated with 1 mol/L NaOH. The formed composites were washed with distilled water until the solution became neutral. Finally the nanocomposites sorbent were dried at 50˚C and ground to powder [<xref ref-type="bibr" rid="scirp.5743-ref28">28</xref>].</p></sec><sec id="s2_3"><title>2.3. Nanocomposites Biosorbent Characterizations</title><p>FTIR spectra of nanocomposites sorbent before and after adsorption of metal ions are recorded in the frequency range of 4000 - 400 cm<sup>–</sup><sup>1</sup> on a Bomen FTIR, MB-series using a Nicolet-5700, Thermo-Nicolet Fourier transform infrared spectrophotometer.</p><p>The X-ray diffraction (XRD) analyses were performed using a diffractometer type D/max-rA (X-650, HITACHI, Japan) with Cu target and Ka radiation (l = 0.154 nm) at 40 kV and 50 mA. The scanning rate was 1˚/min and the scanning scope of 2q was 0.7˚ - 10˚ at room temperature.</p><p>The morphologies of the REC, nanocomposite sorbent (REC/CS = 3:1) were examined using a Hitachi XA-650 scanning electron microscope (SEM; Hitachi, Osaka, Japan). Samples were cryo-fractured from liquid nitrogen, and for morphological studies ﬁlms of samples were mounted on metal grids, using double-sided adhesive tape, and coated with gold under vacuum.</p><p>Ultrathin ﬁlms for transmission electron microscopy (TEM) were prepared by cutting from the epoxy block with the embedded nanocomposite sheet at room temperature using an LKB-8800 ultratome. The TEM micrographs were taken using a transmittance electron microscope [JEM-2010 FEF (UHR), JEOL, Japan] at an accelerating voltage of 200 kV.</p></sec><sec id="s2_4"><title>2.4. Adsorption Experiments</title><p>All batch adsorption experiments were performed on a model KYC-1102 C thermostat shaker (Ningbo, China) with a shaking speed of 100 rpm. Typically, a 50 mL solution of known CHCl<sub>3</sub> concentration and 0.025 g of chitosan/rectorite nanocomposite bioadsorbent were added into 100 mL glass flasks and then shook under 25 &#177; 0.2˚C. At the completion of preset time intervals, the aqueous samples were taken and then filtered. Residual CHCl<sub>3</sub> concentration in supernatant was analyzed at l<sub>max</sub> = 536.0 nm using photolab 6100VIS type spectrophotometer (WTW, Germany). The same procedure has been used to study the effect of initial concentration and pH was adjusted either with 1 M NaOH or 1 M HCl as required. The pH of the solution was measured using a pH meter (Wuxi, China, METTLER TOLEDO-320). Experimental values of CHCl<sub>3</sub> uptake capacities were the results of triplicate experiments reported as means. The concentration retained in the adsorbent phase (q<sub>t</sub>, mg g<sup>–</sup><sup>1</sup>) was calculated by the following equation:</p><p><img src="12-9401349\760be3ee-f576-4d2b-ae3d-7ecc8a812267.jpg" /><img src="12-9401349\70fb748f-ad85-42e8-a475-60bd6b303df0.jpg" /></p><p>where c<sub>o</sub> and c<sub>t </sub>denote the initial and equilibrium CHCl<sub>3</sub> concentrations (mg/L), respectively. ‘v’ was the volume of the solution in liters and ‘m’ was the mass of the adsorbent used (g).</p><p>The removal of CHCl<sub>3</sub>(h) was calculated using the following equation:</p><p><img src="12-9401349\250c1f3c-8401-46c3-bd43-8500233a12b9.jpg" /></p></sec></sec><sec id="s3"><title>3. Results and Discussions</title><sec id="s3_1"><title>3.1. Characterization of Adsorbent</title><sec id="s3_1_1"><title>3.1.1. Fourier Transform Infrared (FTIR) Studies</title><p>As shown in <xref ref-type="fig" rid="fig1">Figure 1</xref>, the FTIR spectra of Na-rectorite sample. The band of 3640 cm<sup>−</sup><sup>1 </sup>corresponds to the frame work water stretching vibrations. At 1630 - 1640 cm<sup>−</sup><sup>1</sup>, there are the bands of flexing vibrations of free water at the edge of clay and in clay holes. The strong band at 1020 cm<sup>−</sup><sup>1</sup> is attributed to Si-O stretching vibrations. Si-O-Al flexing vibration band occurs at about 486 cm<sup>−</sup><sup>1</sup>. The band at about 3440 cm<sup>−</sup><sup>1</sup> is attributed to adsorbed water-flexing vibrations [<xref ref-type="bibr" rid="scirp.5743-ref25">25</xref>]. In the spectra of the nanocomposites, the N-H bonded to O-H vibration band at 3448 cm<sup>–1</sup> in CS shifts towards lower frequency [<xref ref-type="bibr" rid="scirp.5743-ref29">29</xref>], wider and stronger peaks are observed in all the REC/CS nanocomposites. This fact indicates that –NH<sub>2</sub> and –OH groups of CS formed hydrogen bonds with the –OH group in REC which coincided with the CS/MMT nanocomposites [<xref ref-type="bibr" rid="scirp.5743-ref30">30</xref>]. At 1420 cm<sup>−</sup><sup>1</sup> (–NH deformation vibration in –NH<sub>2</sub>), 1027 cm<sup>−</sup><sup>1</sup> (–CO stretching vibration in –COCH<sub>3</sub>), 2877 cm<sup>−</sup><sup>1</sup> (C-H stretching vibration in CS) the peaks at these wave numbers were intact, indicating that the functional groups were not disturbed during the intercalation process. The appearance of all these peaks demonstrates that nanocomposites REC/CS (3:1) had been successfully prepared.</p></sec><sec id="s3_1_2"><title>3.1.2. X-Ray Diffraction (XRD) Studies</title><p>XRD patterns of unmodified REC and XRD pattern of nanocomposites with different REC/CS ratios of 5:1; 3:1 were collected from 0.7˚ to 10˚ (2q) and are show in <xref ref-type="fig" rid="fig2">Figure 2</xref>(a) and (c). It can be observed that unmodified rectorite exhibits 2q = 3.59˚ and the Dd<sub>L</sub> value (the interlayer distance) is 2.45 nm, calculated by the Bragg’s equation [<xref ref-type="bibr" rid="scirp.5743-ref31">31</xref>]. In comparison with REC, the diffraction peaks of the composites rectorite shifted to the small-angle after being intercalated by chitosan, the results indicated that after the chitosan intercalated into the gallery of REC, a new composite material formed. It also can be observed from the <xref ref-type="fig" rid="fig2">Figure 2</xref> that the layer spacing of the composite materials REC and the content of the chitosan was not proportional, when the ratio of amount of chitosan and REC is 1:5, the layer spacing has little change compared to REC merely, but when the ratio is 1:3, the layer spacing achieves to the maximum value of 2.78 nm. Then with the increase of amount of chitosan, the layer spacing is no longer increased, but even tends to decrease, the possible reason is when the content of chitosan is inadequate, the driving force is not enough to carry out the intercalation into the REC. On the contrary, if the content of the chitosan is too much, chitosan molecular structure would be twisted together and wrapped rectorites, resulting in a larger structure, making it difficult to enter the narrow layer of rectories, which make good effects can’t be achieved. So, as the figure shown, when the ratio is 3:1, the effect is best [<xref ref-type="bibr" rid="scirp.5743-ref28">28</xref>].</p></sec><sec id="s3_1_3"><title>3.1.3. Electron Microscope Studies</title><p>The SEM micrographs of REC, nanocomposite biosorbent (b) is shown in <xref ref-type="fig" rid="fig3">Figure 3</xref>. On the SEM of REC (<xref ref-type="fig" rid="fig3">Figure 3</xref>(a)), the surface is smooth, but appears porous. On the SEM of nanocomposite sorbent (REC/CS) (<xref ref-type="fig" rid="fig3">Figure 3</xref>(b)), the chitosan molecule was largely carried on</p><p>the surface of REC, therefore, the surface of the nanocomposite is microporous and have many active groups, But the other part was partly inserted into the REC layer spacing [<xref ref-type="bibr" rid="scirp.5743-ref31">31</xref>], getting through the interlayer hole of rectories, the fluffy surface of nano-composites making the surface area of nanocomposite increases, which increasing its adsorption capacity.</p><p>The TEM micrographs of nanocomposites were observed and are shown in (<xref ref-type="fig" rid="fig3">Figure 3</xref>(c)), it can be seen from the figure, rectories’ structure appears flaky and have many gaps between layers, the chitosan macromolecules distributed in these gaps, observing from TEM, the composite particle appears a size with diameter of tens to hundreds nanometer, so it can be concluded that the composites was nanocomposite materials. Water solution intercalation method directly embed the polymer into the inorganic layer and remove the solution by using appropriate solvent to dissolve polymer and clay, then mixed and stirred to obtain nanocomposites. It also can be seen from TEM analysis, the prepared rectorite/chitosan composites was nanocomposite materials, the result was consistent with the water solution interaction technique [<xref ref-type="bibr" rid="scirp.5743-ref28">28</xref>].</p></sec></sec><sec id="s3_2"><title>3.2. Adsorption Studies</title><sec id="s3_2_1"><title>3.2.1. Comparison of CHCl<sub>3</sub> Adsorption with Different Adsorbent</title><p><xref ref-type="fig" rid="fig4">Figure 4</xref> shows adsorption percent of CHCl<sub>3</sub> as a function of contact time onto four different adsorbents, namely rectories (a), chitosan (b), REC:CS 5:1 (c), REC/CS 3:1 (d), respectively. The saturation adsorption capacities of CHCl<sub>3</sub> onto the four adsorbents were measured as 25 mg&#183;g<sup>–</sup><sup>1</sup>, 51 mg&#183;g<sup>–</sup><sup>1</sup>, 73.6 mg&#183;g<sup>–</sup><sup>1</sup> and 81 mg&#183;g<sup>–</sup><sup>1</sup>, respectively. The data indicated that the two REC/CS adsorbents showed higher adsorption capacities as compared with those of rectories and chitosan. On one hand, due to the intercalation of polymer chains usually increases the interlayer spacing relative to that of the pure REC [<xref ref-type="bibr" rid="scirp.5743-ref32">32</xref>], on the other hand, the introduction of chitosan, provided more available sites for CHCl<sub>3</sub> adsorption due to a larger surface and smaller pore diameter compared with rectories [<xref ref-type="bibr" rid="scirp.5743-ref33">33</xref>]. The phenomenon has been proved by the result of XRD and SEM analysis.</p><p>At the same time, it took 100 min, 80 min, 40 min and 50 min to attain equilibrium for rectories, chitosan, REC/CS 3:1 and REC:CS 5:1, respectively. The CHCl<sub>3</sub> removal increased dramatically and the adsorption equilibrium was achieved much faster with the introduction of chitosan. From the experimental data, it is observed that by introducing inorganic REC particles into the polymeric networks, the adsorption capacity seems to be affected significantly, especially in different time. This behavior is very clear. Nevertheless, one can conclude that this nanocomposite can be used in a wide short equilibration time.</p></sec><sec id="s3_2_2"><title>3.2.2. Effect of Initial pH Values on CHCl<sub>3</sub> Adsorption Capacity</title><p>Generally, the solution pH values are one of the important parameters controlling the adsorption of CHCl<sub>3</sub> from aqueous solution onto solid polymeric adsorbent [<xref ref-type="bibr" rid="scirp.5743-ref34">34</xref>]. In order to investigated effect of initial solution pH values on CHCl<sub>3</sub> removal, experiments were carried out using various pH levels in the range of 4.0 - 9.0, as shown in <xref ref-type="fig" rid="fig5">Figure 5</xref>. It appears that the adsorption percent of CHCl<sub>3</sub> onto 3:1 REC/CS decreased from 81.8% to 22.0% after 60 min adsorption with increase in pH from 4.0 to 9.0. This result indicated that the adsorption capacity decreased with the increase of initial solution pH. The decrease of chloroform adsorption with increasing pH can be explained by the electrostatic interaction between the adsorbent surface and the CHCl<sub>3</sub>. Because chitosan has a positively charged surface below pH 6.5 (point of zero potential). In acidic solution, hydrogen atoms (H<sup>+</sup>) in solution can protonate amine groups (–NH<sub>2</sub>) of chitosan. As a result, the electrostatic interactions between CHCl<sub>3</sub> and chitosan with positively charged surface increased in acidic solution [<xref ref-type="bibr" rid="scirp.5743-ref35">35</xref>].</p></sec><sec id="s3_2_3"><title>3.2.3. Effects of Adsorbent Dosage on CHCl<sub>3</sub> Adsorption Capacity</title><p>Adsorption dosage is another important parameter because it determines the capacity of an adsorbent for a given initial concentration of adsorbate. Effect of adsorbent dosage was studied on CHCl<sub>3</sub> removal from aqueous solutions by varying the amount of 3:1 REC/CS from 0.1 g&#183;L<sup>–</sup><sup>1</sup> to 0.7 g&#183;L<sup>–</sup><sup>1</sup> while keeping other parameters constant such as 50 mg&#183;L<sup>−1</sup> initial CHCl<sub>3</sub> concentration, initial solution pH 6.8 and stirring rate 120 rpm. The CHCl<sub>3</sub> removal increased from 12.1% to 81.2% with increasing adsorbent dosage from 0.1&#183;g L<sup>−1</sup> to 0.7 g&#183;L<sup>−1 </sup>(<xref ref-type="fig" rid="fig6">Figure 6</xref>). Initially, a rapid increase of adsorption with the increasing adsorbent dosage was attributed to availability of more adsorption sites [<xref ref-type="bibr" rid="scirp.5743-ref36">36</xref>]. However, further increase in adsorbent dosage to 0.7 g&#183;L<sup>−1</sup> only leads to the adsorption percent increase by 0.2%. At the same time, the amount adsorbed (q<sub>e</sub>) decreased from 60 mg&#183;g<sup>−1</sup> to 57.6 mg&#183;g<sup>−1</sup> when the adsorbent dosage increased from 0.1 g&#183;L<sup>−1</sup> to 0.7 g&#183;L<sup>−1</sup>. The decrease of adsorption was due to the concentration gradient between adsorbent and adsorptive [<xref ref-type="bibr" rid="scirp.5743-ref37">37</xref>]. As a result, 0.5 g&#183;L<sup>−1</sup> was the optimum adsorbent dosage for CHCl<sub>3</sub> adsorption onto 3:1 REC/CS. This result was in agreement with the XRD analysis.</p></sec></sec></sec><sec id="s4"><title>4. Conclusions</title><p>A new nanocomposite adsorbent was prepared and characterized using the FTIR, XRD, SEM, TEM. The nanocomposite adsorbents for CHCl<sub>3</sub> from aqueous solution were tested. The following conclusions can be made from this study:</p><p>1) The results confirm that when the ratio of the rectorite and chitosan is 3:1, the pH of the solution is 6.8, the adsorption time is 40 min, the dosage is 0.5 g/L and the temperature is 30℃, the adsorption capacity of CHCl<sub>3</sub> onto nanocomposites were largest.</p><p>2) According to the comparison made with CS, REC adsorption efficiency on CHCl<sub>3</sub>, nanocomposite adsorbent on CHCl<sub>3</sub> adsorption capacity significantly increased.&#160;</p></sec><sec id="s5"><title>5. Acknowledgements</title><p>The authors thank for jointly supporting by the National Natural Science Foundation of China (20577036, 20777058, 20977070) and “863” Project of the Ministry of Science and Technology, PR China (2007AA06Z418).</p></sec><sec id="s6"><title>REFERENCES</title></sec></body><back><ref-list><title>References</title><ref id="scirp.5743-ref1"><label>1</label><mixed-citation publication-type="other" xlink:type="simple">S. O_Doherty, P. G. Simmonds, D. M. Cunnold, H. J. Wang, G. A. Sturrock, P. J. Fraser, D. Ryall, R. G. Derwent, R. F. Weiss, P. Salameh, B. R. Miller and R. G. Prinn, “In situ Chloroform Measurements at Advanced Global Atmospheric Gases Experiment Atmospheric Research Stations from 1994 to 1998,” Journal of Geophysics Research, Vol. 106, No. (D17), 2001, pp. 20429- 20444.</mixed-citation></ref><ref id="scirp.5743-ref2"><label>2</label><mixed-citation publication-type="other" xlink:type="simple">S. Zok, J. -C. Boutonnet, C. de Rooij, V. Garny, A. 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